<?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">JSEMAT</journal-id><journal-title-group><journal-title>Journal of Surface Engineered Materials and Advanced Technology</journal-title></journal-title-group><issn pub-type="epub">2161-4881</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jsemat.2015.52011</article-id><article-id pub-id-type="publisher-id">JSEMAT-55236</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Chemistry&amp;Materials Science</subject><subject> Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Preparation, Characterization and Catalytic Activity of Alkyl Benzene Sulfonic Acid Carbon-Based Acid Catalyst
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Huoxin</surname><given-names>Luan</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Yunqiang</surname><given-names>Wu</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Wenxiang</surname><given-names>Wu</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Quansheng</surname><given-names>Chen</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Hailing</surname><given-names>Zhang</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Kang</surname><given-names>Liu</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Guangmiao</surname><given-names>Qu</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Wei</surname><given-names>Ding</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Xinjiang Oilfield Company, Xinjiang, China</addr-line></aff><aff id="aff2"><addr-line>Northeast Petroleum University, Daqing, China</addr-line></aff><pub-date pub-type="epub"><day>03</day><month>02</month><year>2015</year></pub-date><volume>05</volume><issue>02</issue><fpage>93</fpage><lpage>101</lpage><history><date date-type="received"><day>3</day>	<month>March</month>	<year>2015</year></date><date date-type="rev-recd"><day>accepted</day>	<month>26</month>	<year>March</year>	</date><date date-type="accepted"><day>31</day>	<month>March</month>	<year>2015</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>
 
 
  Based on starch and series of alkyl benzene sulfonic acid as the materials, a novel carbon-based solid acid catalyst is synthesized using hydrothermal method. This catalyst exhibits much higher catalytic activity in the reaction of esterification of Mono-fatty alcohol polyoxyethylene maleate esters with 1,4-butanediol. The structure of carbon-based solid acid catalyst was charactered by IR and XRD, characterizations showed that this catalyst exhibited high –SO3H loading. Reusability of the carbon-based solid acid catalyst for esterification showed that after recycling five times the activity remained unchanged.
 
</p></abstract><kwd-group><kwd>Alkyl Benzene Sulfonic Acid</kwd><kwd> Carbon-Based Solid Acid Catalyst</kwd><kwd> Esterification</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>The principles of green chemistry and increasing concerns about environmental issues have stimulated the research for recyclable strong solid acids to replace of conventional toxic and corrosive acid catalysts, such as sulfuric acid [<xref ref-type="bibr" rid="scirp.55236-ref1">1</xref>] . Integration of acidic functional groups (e.g., ?SO<sub>3</sub>H) into solid surface, e.g. carbonaceous [<xref ref-type="bibr" rid="scirp.55236-ref2">2</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref5">5</xref>] or silica-based materials [<xref ref-type="bibr" rid="scirp.55236-ref6">6</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref9">9</xref>] , has been explored to produce promising solid acids. Among them, the sulfonated carbon materials have received much attention due to their low costs, high stability, and high activities. Sulfonated carbonaceous materials were usually synthesized through the oxidation of carbon materials by sulfur acid [<xref ref-type="bibr" rid="scirp.55236-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.55236-ref12">12</xref>] or oleum [<xref ref-type="bibr" rid="scirp.55236-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.55236-ref14">14</xref>] to generate sulfonic acid groups on the surface. For example, Hara et al. [<xref ref-type="bibr" rid="scirp.55236-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.55236-ref11">11</xref>] obtained a series of carbon-based catalysts with acid densities ranging from 0.37 to 1.34 mmol H<sup>+</sup>/g by the sulfonation of incompletely carbonized sugars. Similarly, Budarin et al. [<xref ref-type="bibr" rid="scirp.55236-ref12">12</xref>] synthesized a mesoporous sulfonated Starbon-400 with 0.5 mmol/g SO<sub>3</sub>H loading. An ordered mesoporous phenol-formaldehyde resin [<xref ref-type="bibr" rid="scirp.55236-ref14">14</xref>] was also functionalized with sulfonate groups by putting the material in the vapor of fuming sulfuric acid inside an autoclave. Ryoo et al. [<xref ref-type="bibr" rid="scirp.55236-ref15">15</xref>] synthesized an ordered mesoporous carbons (OMCs) through the nanocasting technique using OMCS as templatesor via self-assembly of phenolic resins and block copolymers [<xref ref-type="bibr" rid="scirp.55236-ref16">16</xref>] [<xref ref-type="bibr" rid="scirp.55236-ref17">17</xref>] . These materials exhibit high surface area, narrow pore size distribution, and large pore volume. Recently, a new class of sulfonated carbons (C-SO<sub>3</sub>H) derived from the incomplete carbonization of simple sugars and starch were reported to show excellent catalytic performance for the synthesis of biodiesel [<xref ref-type="bibr" rid="scirp.55236-ref18">18</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref20">20</xref>] .</p></sec><sec id="s2"><title>2. Experiment Procedures</title><p>Alkyl benzene sulfonic acid was synthesized according to the literature; fatty alcohol polyoxyethylene ether (AEO-3) was from Liao Yang Oak polyether Co., Ltd. (Liaoyang, Liaoning Province, China). The catalyst was synthesized according to the literature. Maleic anhydride (MAH) was obtained from Kemiou (Tianjin, China). Nitrogen was of high grade purity from Xue Long (99.99% purity, Daqing, China). The IR spectra was obtained on a 4300 Shimadzu spectrophotometer as KBr disks. XRD (Rigaku, Tokyo, Japan).</p><sec id="s2_1"><title>2.1. Synthesis of Alkyl Benzene Sulfonic Acid</title><p>The synthesis procedure of alkyl benzene sulfonic acid is as shown in the References [<xref ref-type="bibr" rid="scirp.55236-ref21">21</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref24">24</xref>] , and the molecular structure of alkyl aryl benzene sulfonic acid as following in Scheme 1.</p></sec><sec id="s2_2"><title>2.2. Synthesis of the Carbon-Based Solid Acid Catalyst</title><p>In typical procedure: 15 g starch and 15 g sulfonic acid were mixed together and transferred to the quartz furnace. The mixture was heated to 200˚C from room temperature with the heating rate of 1˚C/min and remained at 200˚C for 12 h under nitrogen atmosphere. After cooling to room temperature, obtained black solid was washed with deionized water until no acidity detected in the filtrate. The novel solid acid was obtained after drying at 120˚C overnight in an oven and grinding it into fine flour. P-toluene sulphonic acid carbon-based solid acid catalyst, tetradecyl benzene sulphonic acid carbon-based solid acid catalyst, hexadecyl benzene sulphonic acid carbon-based solid acid catalyst and octadecyle benzene sulphonic acid carbon-based solid acid catalyst are abbreviated in what follows as cat 1, cat 2, cat 3, cat 4 respectively.</p></sec><sec id="s2_3"><title>2.3. Synthesis of Mono-Fatty Alcohol Polyoxyethylene Maleate Esters</title><p>Mono-fatty alcohol polyoxyethylene maleate esters were synthesized by 0.1 mol (9.806 g) of maleic anhydride (MAH) reacted to 0.1 mol (31.695 g, M = 317.695 g/mol) of fatty alcohol polyoxyethylene (AEO-3) and 0.1% (wt) p-toluene sulphonic acid served as a catalyst for 8 h with heating at 80˚C. Standard titration solution of NaOH was used to determine the system acid value, and when the variation of acid value was less than 1 mg/h, it was regarded as near the end point of esterification. The crude product was recrystallized from ethanol and water (V/V = 1:1) to three times. Compound 1a was obtained in 95.66%.</p></sec><sec id="s2_4"><title>2.4. Synthesis of Bis(Mono-Fatty Alcohol Polyoxyethylene Maleate)1,4-Butanediol Ester</title><p>0.05 mol (20.515 g) of compound 1 reacted with 0.025 mol (2.253 g) of 1,4-butanediol and 1% (wt) of carbon- based solid acid served as catalyst under vacuum degree of −0.09 mpa at 150˚C reacting 10 h. and real-time detection of acid value. The esterification rate was calculated using the following formula [<xref ref-type="bibr" rid="scirp.55236-ref25">25</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref27">27</xref>] : (Er) = (1-</p><disp-formula id="scirp.55236-formula240"><graphic  xlink:href="http://html.scirp.org/file/5-1180278x5.png"  xlink:type="simple"/></disp-formula><p>Scheme 1. The molecular structure of alkyl aryl benzene sulfonic acid.</p><p>AV<sub>a</sub>/AV<sub>b</sub>) &#215; 100%, where Er is esterification rate, AV<sub>a</sub> is Final acid value, AV<sub>b</sub> is Initial acid value. The typical procedure (Scheme 2).</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><p>The reaction mechanism is most probably like this: Firstly, the starch was dehydrated into small organic molecules, mainly 5-(hydroxymethyl)-2-furaldehyde (HMF) [<xref ref-type="bibr" rid="scirp.55236-ref28">28</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref30">30</xref>] , and the generated HMF could be hydrothermally carbonized into a carbon-rich resin as well as react with alkyl benzene sulfonic acid to “embed” sulfonic acid groups as is shown in Scheme 3.</p><sec id="s3_1"><title>3.1. Characterization of Carbon-Based Solid Acid Catalyst</title><p>The FT-IR spectrum <xref ref-type="fig" rid="fig1">Figure 1</xref> showed that the carbon-based solid acid contain resident functionalities including,</p><disp-formula id="scirp.55236-formula241"><graphic  xlink:href="http://html.scirp.org/file/5-1180278x6.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.55236-formula242"><graphic  xlink:href="http://html.scirp.org/file/5-1180278x7.png"  xlink:type="simple"/></disp-formula><p>Cat 1: p-toluene sulphonic acid catalyst, Cat 2: tetradecyl benzene sulphonic acid catalyst</p><p>Cat 3: hexadecyl benzene sulphonic acid catalyst, Cat 4: octadecyle benzene sulphonic acid catalyst</p><p>Scheme 2. Synthesis route of the reaction.</p><disp-formula id="scirp.55236-formula243"><graphic  xlink:href="http://html.scirp.org/file/5-1180278x8.png"  xlink:type="simple"/></disp-formula><p>Scheme 3. Hydrothermal method to synthesis of carbon-based solid acid.</p><p>1007 cm<sup>−1</sup>, 1032 cm<sup>−1</sup> (S=O str). 1118 cm<sup>−1</sup> (SO<sub>3</sub>H str), 1710 cm<sup>−1</sup> (C=O bend), 3450 cm<sup>−1</sup> (OH str) On the other hand, the bands due to ?OH stretching at 3420 cm<sup>−</sup><sup>1</sup>, and C=C bonds stretching at 1620 cm<sup>−</sup><sup>1</sup> were observed for both samples independent of the sulfonation. It is shown that the carbon-based solid acid have the group of -SO<sub>3</sub>H.</p><p>The XRD pattern (<xref ref-type="fig" rid="fig2">Figure 2</xref>) contains two broad and weak diffraction peaks C (002) diffraction peak (2θ = 10˚ - 35˚) attributable to amorphous carbon composed of aromatic carbon sheets oriented in a considerably ran</p><fig-group id="fig1"><label><xref ref-type="fig" rid="fig1">Figure 1</xref></label><caption><title> FT-IR spectrum of carbon-based solid acid.</title></caption><fig id ="fig1_1"><label></label><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/5-1180278x9.png"/></fig></fig-group><fig-group id="fig2"><label><xref ref-type="fig" rid="fig2">Figure 2</xref></label><caption><title> XRD of carbon-based solid acid XRD (Rigaku, Tokyo, Japan).</title></caption><fig id ="fig2_1"><label></label><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/5-1180278x10.png"/></fig></fig-group><p>dom fashion. A definitive C (101) diffraction peak (2θ = 35˚ - 45˚) due to the a axis of the graphite structure can be seen. The X-ray diffractogram is similar to that of char because the sulfonic acid groups were attached to edges of isotropic carbon sheets and the solid acid exhibits broad diffraction peaks of amorphous carbon [<xref ref-type="bibr" rid="scirp.55236-ref31">31</xref>] - [<xref ref-type="bibr" rid="scirp.55236-ref33">33</xref>] .</p></sec><sec id="s3_2"><title>3.2. Qrthogonal Experiment of Cat 1 Carbon-Based Solid Acid</title><p>The optimum reaction conditions from <xref ref-type="table" rid="table1">Table 1</xref> was obtained as follows: m<sub>starch</sub>:m<sub>cat 1</sub> = 1:1, reaction temperature: 220˚C, reaction time: 10 h, All results were repeated for three times: Esterification rate were 91.85%, 90.63% and 90.71% respectively, average value was 91.06%.</p></sec><sec id="s3_3"><title>3.3. Qrthogonal Experiment of Cat 2 Carbon-Based Solid Acid</title><p>The optimum reaction conditions from <xref ref-type="table" rid="table2">Table 2</xref> was obtained as follows: reaction temperature: 180˚C; reaction</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Qrthogonal experiment of Cat 1 carbon-based solid acid</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Factor</th><th align="center" valign="middle" >Temperature/˚C</th><th align="center" valign="middle" >Hour/h</th><th align="center" valign="middle" >m<sub>starch</sub>:m<sub>cat1</sub><sup>*</sup></th><th align="center" valign="middle" >Esterification rate/%</th></tr></thead><tr><td align="center" valign="middle" >Experiment 1</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >91.57</td></tr><tr><td align="center" valign="middle" >Experiment 2</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >90.49</td></tr><tr><td align="center" valign="middle" >Experiment 3</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >1:</td><td align="center" valign="middle" >85.88</td></tr><tr><td align="center" valign="middle" >Experiment 4</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >87.13</td></tr><tr><td align="center" valign="middle" >Experiment 5</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >88.65</td></tr><tr><td align="center" valign="middle" >Experiment 6</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >90.12</td></tr><tr><td align="center" valign="middle" >Experiment 7</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >87.12</td></tr><tr><td align="center" valign="middle" >Experiment 8</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >85.89</td></tr><tr><td align="center" valign="middle" >Experiment 9</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >91.72</td></tr><tr><td align="center" valign="middle" >Average 1</td><td align="center" valign="middle" >88.607</td><td align="center" valign="middle" >89.193</td><td align="center" valign="middle" >89.313</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 2</td><td align="center" valign="middle" >88.343</td><td align="center" valign="middle" >89.780</td><td align="center" valign="middle" >88.633</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 3</td><td align="center" valign="middle" >89.240</td><td align="center" valign="middle" >87.217</td><td align="center" valign="middle" >88.243</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Standard deviation</td><td align="center" valign="middle" >0.897</td><td align="center" valign="middle" >2.563</td><td align="center" valign="middle" >1.070</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p><sup>*</sup>Average 1 is experiments 1, 4, 7; Average 2 is 2, 5, 8; Average 3 is 3, 6, 9.</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Qrthogonal experiment of Cat 2 carbon-based solid acid</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Factor</th><th align="center" valign="middle" >Temperature/˚C</th><th align="center" valign="middle" >Hour/h</th><th align="center" valign="middle" >m<sub>starch</sub>:m<sub>cat2</sub></th><th align="center" valign="middle" >Esterification rate/%</th></tr></thead><tr><td align="center" valign="middle" >Experiment 1</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >93.92</td></tr><tr><td align="center" valign="middle" >Experiment 2</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >90.82</td></tr><tr><td align="center" valign="middle" >Experiment 3</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >88.52</td></tr><tr><td align="center" valign="middle" >Experiment 4</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >90.27</td></tr><tr><td align="center" valign="middle" >Experiment 5</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >89.99</td></tr><tr><td align="center" valign="middle" >Experiment 6</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >89.35</td></tr><tr><td align="center" valign="middle" >Experiment 7</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >71.17</td></tr><tr><td align="center" valign="middle" >Experiment 8</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >88.15</td></tr><tr><td align="center" valign="middle" >Experiment 9</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >85.98</td></tr><tr><td align="center" valign="middle" >Average 1</td><td align="center" valign="middle" >91.087</td><td align="center" valign="middle" >85.120</td><td align="center" valign="middle" >90.473</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 2</td><td align="center" valign="middle" >89.870</td><td align="center" valign="middle" >89.653</td><td align="center" valign="middle" >89.023</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 3</td><td align="center" valign="middle" >81.767</td><td align="center" valign="middle" >87.950</td><td align="center" valign="middle" >83.227</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Standard deviation</td><td align="center" valign="middle" >9.320</td><td align="center" valign="middle" >4.533</td><td align="center" valign="middle" >7.246</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p><sup>*</sup>Average 1 is experiments 1, 4, 7; Average 2 is 2, 5, 8; Average 3 is 3, 6, 9.</p><p>time: 10 h; m<sub>starch</sub>:m<sub>cat2</sub> = 1:1, All results were repeated for three times: Esterification rate were 88.04%, 86.98% and 90.82%, average value was 88.61%.</p></sec><sec id="s3_4"><title>3.4. Qrthogonal Experiment of Cat 3 Carbon-Based Solid Acid</title><p>The optimum reaction conditions from <xref ref-type="table" rid="table3">Table 3</xref> was obtained as follows: reaction temperature: 220˚C, reaction time: 10 h, m<sub>starch</sub>:m<sub>cat3 </sub>= 1:3, All results were repeated for three times: Esterification rate were 91.08%, 89.42% and 89.92%, average value was 90.14%.</p></sec><sec id="s3_5"><title>3.5. Qrthogonal Experiment of Cat 4 Carbon-Based Solid Acid</title><p>The optimum reaction conditions from <xref ref-type="table" rid="table4">Table 4</xref> was obtained as follows: reaction temperature: 180˚C; reaction time: 12 h; m<sub>starch</sub>:m<sub>cat4</sub> = 1:1, All results were repeated for three times: Esterification rate were 90.07%, 91.98% and 93.06%, average value was 91.70%.</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Qrthogonal experiment of Cat 3 carbon-based solid acid</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Factor</th><th align="center" valign="middle" >Temperature/˚C</th><th align="center" valign="middle" >Hour/h</th><th align="center" valign="middle" >m<sub>starch</sub>:m<sub>cat3</sub></th><th align="center" valign="middle" >Esterification rate/%</th></tr></thead><tr><td align="center" valign="middle" >Experiment 1</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >80.02</td></tr><tr><td align="center" valign="middle" >Experiment 2</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >81.18</td></tr><tr><td align="center" valign="middle" >Experiment 3</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >84.11</td></tr><tr><td align="center" valign="middle" >Experiment 4</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >80.38</td></tr><tr><td align="center" valign="middle" >Experiment 5</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >80.94</td></tr><tr><td align="center" valign="middle" >Experiment 6</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >77.39</td></tr><tr><td align="center" valign="middle" >Experiment 7</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >90.23</td></tr><tr><td align="center" valign="middle" >Experiment 8</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >90.67</td></tr><tr><td align="center" valign="middle" >Experiment 9</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >91.29</td></tr><tr><td align="center" valign="middle" >Average 1</td><td align="center" valign="middle" >81.770</td><td align="center" valign="middle" >83.543</td><td align="center" valign="middle" >82.693</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 2</td><td align="center" valign="middle" >79.570</td><td align="center" valign="middle" >84.263</td><td align="center" valign="middle" >84.283</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 3</td><td align="center" valign="middle" >90.730</td><td align="center" valign="middle" >84.263</td><td align="center" valign="middle" >85.093</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Standard deviation</td><td align="center" valign="middle" >11.160</td><td align="center" valign="middle" >0.720</td><td align="center" valign="middle" >2.400</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p><sup>*</sup>Average 1 is experiments 1, 4, 7; Average 2 is 2, 5, 8; Average 3 is 3, 6, 9.</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Qrthogonal experiment of Cat 4 carbon-based solid acid</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Factor</th><th align="center" valign="middle" >Temperature/˚C</th><th align="center" valign="middle" >Hour/h</th><th align="center" valign="middle" >m<sub>starch</sub>:m<sub>cat4</sub></th><th align="center" valign="middle" >Esterification rate/%</th></tr></thead><tr><td align="center" valign="middle" >Experiment 1</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >89.11</td></tr><tr><td align="center" valign="middle" >Experiment 2</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >89.68</td></tr><tr><td align="center" valign="middle" >Experiment 3</td><td align="center" valign="middle" >180</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >91.26</td></tr><tr><td align="center" valign="middle" >Experiment 4</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >90.1</td></tr><tr><td align="center" valign="middle" >Experiment 5</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >83.84</td></tr><tr><td align="center" valign="middle" >Experiment 6</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >90.53</td></tr><tr><td align="center" valign="middle" >Experiment 7</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >3:1</td><td align="center" valign="middle" >86.9</td></tr><tr><td align="center" valign="middle" >Experiment 8</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >91.93</td></tr><tr><td align="center" valign="middle" >Experiment 9</td><td align="center" valign="middle" >220</td><td align="center" valign="middle" >12</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >87.81</td></tr><tr><td align="center" valign="middle" >Average 1</td><td align="center" valign="middle" >90.017</td><td align="center" valign="middle" >88.703</td><td align="center" valign="middle" >90.523</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 2</td><td align="center" valign="middle" >88.157</td><td align="center" valign="middle" >88.483</td><td align="center" valign="middle" >89.197</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Average 3</td><td align="center" valign="middle" >88.880</td><td align="center" valign="middle" >89.867</td><td align="center" valign="middle" >87.333</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >Standard deviation</td><td align="center" valign="middle" >1.860</td><td align="center" valign="middle" >1.384</td><td align="center" valign="middle" >3.190</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p><sup>*</sup>Average 1 is experiments 1, 4, 7; Average 2 is 2, 5, 8; Average 3 is 3, 6, 9.</p></sec><sec id="s3_6"><title>3.6. Comparison of Catalytic Activities</title><p>The esterification at 0.05 mol (20.515 g) of compound 1a reacted to 0.025 mol (2.253g) of 1,4-butanediol and 1% (wt) of carbon-based solid acid was used as catalyst under vacuum degree of −0.09 mpa at 150˚C reacting 10 h. From <xref ref-type="fig" rid="fig3">Figure 3</xref> we can see that alkyl benzene sulfonic acid carbon-based solid acid catalyst (cat2, cat3, cat4) has the same catalytic activity with p-toluene sulphonic acid carbon-based solid acid catalyst (cat1) in the reaction of esterification of Mono-fatty alcohol polyoxyethylene maleate esters with 1,4-butanediol.</p><p>The reusability of the alkyl benzene sulfonic acid carbon-based solid acid catalyst was investigated for the reaction of esterification. After the reaction had reached equilibrium, the novel carbon-based acid was simply recovered by filtration and recycled for further reaction. It was confirmed that the activity remained unchanged, even after the catalyst had been recycled five times (<xref ref-type="fig" rid="fig4">Figure 4</xref>).</p><fig id="fig3"  position="float"><label><xref ref-type="fig" rid="fig3">Figure 3</xref></label><caption><title> Catalytic activity</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/5-1180278x11.png"/></fig><fig id="fig4"  position="float"><label><xref ref-type="fig" rid="fig4">Figure 4</xref></label><caption><title> Reusability of carbon-based solid acid catalyst for esterification</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/5-1180278x12.png"/></fig></sec></sec><sec id="s4"><title>4. Conclusion</title><p>A novel and facile method for preparing highly active carbon-based solid-acid catalyst functionalized with sulfonic acid groups was reported. In this method, alkyl benzene sulfonic acid was used in the synthesis instead of concentrated/fuming sulfur acid and the preparation was made safer by avoiding usage of dangerous chemicals. The so-prepared catalyst exhibits much higher catalytic activity in the reaction of esterification of Mono-fatty alcohol polyoxyethylene maleate esters with 1,4-butanediol. The cycle usage test indicated that the catalyst prepared by this method was relative stable.</p></sec><sec id="s5"><title>Acknowledgements</title><p>This research was financially supported by the National Key Basic Research Development Program (2005- CB221305), the National Natural Science Foundation of China (No. 50174033).</p></sec><sec id="s6"><title>Cite this paper</title><p>Gaalya, M.S., Ed- ward, B. and Eria, H. (2017) Trade Openness and Tax Revenue Performance in East African Countries. 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