<?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">GSC</journal-id><journal-title-group><journal-title>Green and Sustainable Chemistry</journal-title></journal-title-group><issn pub-type="epub">2160-6951</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/gsc.2015.52009</article-id><article-id pub-id-type="publisher-id">GSC-55816</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></subj-group></article-categories><title-group><article-title>
 
 
  Research on Extraction Process of Gallic Acid from &lt;i&gt;Penthorum chinense&lt;/i&gt; Pursh by Aqueous Ethanol
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>uping</surname><given-names>Kang</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>Shanbin</surname><given-names>Yang</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Yan</surname><given-names>Peng</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>Jiao</surname><given-names>Dai</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>Xingchun</surname><given-names>Ying</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Pharmaceutical Engineering Institute of Engineering Research Center of Biotechnology of Active Materials (Ministry of Education) in Chongqing Normal University, Chongqing, China</addr-line></aff><aff id="aff2"><addr-line>Key Laboratory of Green Synthesis and Applications, College of Chemistry, Chongqing Normal University, Chongqing, China</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>shanbiny@126.com(SY)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>08</day><month>04</month><year>2015</year></pub-date><volume>05</volume><issue>02</issue><fpage>63</fpage><lpage>69</lpage><history><date date-type="received"><day>19</day>	<month>February</month>	<year>2015</year></date><date date-type="rev-recd"><day>accepted</day>	<month>14</month>	<year>April</year>	</date><date date-type="accepted"><day>20</day>	<month>April</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>
 
 
  Penthorum chinense Pursh is rich in gallic acid, which has antioxidant, anti-inflammatory, anti-fungal and antitumor activities. In order to optimize their extraction conditions, various extraction parameters were chosen to identify their effects on gallic acid extraction. With extraction amount of gallic acid as index, based on single factor analysis, influence of solid/liquid ratio, ethanol concentration, fetch time and extraction temperature on extraction technology were investigated by orthogonal test. The optimization conditions for gallic acid extraction were determined as follows: ethanol concentration 60%, extraction time 2.5 h, temperature 90
  &#176;C and solid/liquid ratio 1:30. The corresponding gallic acid content was 4.85%. This optimized extraction process was stable and feasible.
 
</p></abstract><kwd-group><kwd>Penthorum</kwd><kwd> Gallic Acid</kwd><kwd> Extraction Process</kwd><kwd> Orthogonal Design</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Penthorum chinense Pursh is the species belonging to Saxifragaceae Penthorum perennial herb, and the whole plant is popularly used as medicine in china. It is mainly distributed in Hunan, Sichuan and Guizhou and other provinces. It is a rooted vascular plant, which has the functions of detoxification, diuresis, and promoting blood circulation. In addition, abundant studies have shown that they have anti-aging, anti-viral, anti-mutation activities [<xref ref-type="bibr" rid="scirp.55816-ref1">1</xref>] . The chemical investigations on P. chinense revealed the occurrence of molecules such as flavonoids, gallic acid, sitosterol, organic acid, volatile oil, the major constituents of which are flavonoids and gallic acid [<xref ref-type="bibr" rid="scirp.55816-ref2">2</xref>] . Gallic acid is a hydrolysable tannin monomer, which has the effect of anti-viral and protecting liver [<xref ref-type="bibr" rid="scirp.55816-ref3">3</xref>] -[<xref ref-type="bibr" rid="scirp.55816-ref5">5</xref>] . Extraction flavonoids from P. chinense were studied by determining the content of quercetin, quercitrin and gallic acid with HPLC [<xref ref-type="bibr" rid="scirp.55816-ref6">6</xref>] [<xref ref-type="bibr" rid="scirp.55816-ref7">7</xref>] . In this paper, gallic acid from Penthorum chinense pursh extracted with aqueous ethanol was studied. With extraction amount of gallic acid as index, based on single factor analysis, influence of solid/liquid ratio, ethanol concentration, fetch time and extraction temperature on extraction technology was investigated by orthogonal test. The content of gallic acid was determined by ultraviolet?visible spectroscopy. It was conveninent and fast for quality control in actual manufacturing.</p></sec><sec id="s2"><title>2. Materials and Equipment</title><sec id="s2_1"><title>2.1. Reagents</title><p>Dried Penthorum chinense Pursh was purchased from Gulin Hongan Pharmaceutical Company (Sichuan Province, China). gallic acid (reference standard) was purchased from National Instisutes for Food and Drug Control in China; all the other chemicals used were of analytical grade.</p></sec><sec id="s2_2"><title>2.2. General Instrumental Equipment</title><p>An electronic balance was measured on quality (Jingtian electronic instrument company, Shanghai, China, JT202N); An UV-vis spectrophotometer was used for quantification of gallic acid (Analysis of general instrument company, Beijing, China, T6)</p></sec></sec><sec id="s3"><title>3. Methods and Results</title><sec id="s3_1"><title>3.1. Determination of Gallic Acid Content</title><p>Gallic acid standard substance (25.4 mg) was accurately weighed, dissolved and filled into a 100 mL volumetric flask. Then 60% ethanol was added into the volumetric flask. 0.0 mL, 1.0 mL, 2.0 mL, 3.0 mL, 4.0 mL, 5.0 mL from 100 mL volumetric flask was filled into 6 volumetric flasks, respectively. Then 60% ethanol was added into these volumetric flasks and stood for 10 minutes in dark place. At last, absorbance values were recorded by a T6 spectrophotometer at the wavelength of 279 nm. At the same time, the 60% ethanol was measured as blank control in an identical way. The regression equation of the gallic acid standard curve was obtained as A = 50.098C + 0.1587 (R<sup>2</sup> = 0.9946), exhibiting a good linear relationship within the rang of 0.005 - 0.025 mg∙mL<sup>−1</sup> (see <xref ref-type="fig" rid="fig1">Figure 1</xref>).</p></sec><sec id="s3_2"><title>3.2. Gallic Acid Samples and Preparation of Penthorum chinense Pursh Extract</title><p>Penthorum chinense Pursh (6.0 g) was treated by water bath for extraction of gallic acid under the designed conditions. Extraction conditions were adjusted to different ethanol concentrations (30% - 80%), ratios of solid/liquid (g∙mL<sup>−1</sup>) (1:10 - 1:35), extraction times (1 - 3.5 h), and water bath temperatures (50˚C - 100˚C). When one of the conditions was changed, the other conditions were adjusted accordingly. Penthorum chinense Pursh was extracted twice. After the extracts were combined and filtered, the obtained concentrated solution was dissolved in ethanol (60%) to 200 mL, then, 2.0 mL was taken out to a defined volume of 50 mL for analysis.</p></sec><sec id="s3_3"><title>3.3. Precision Experiment</title><p>3.0 mL from the standard solution was filled into 50 mL volumetric falsk, measured 6 times according to the method of 2.1, RSD = 1.02%. The precision of this method was good.</p></sec><sec id="s3_4"><title>3.4. Stability Test</title><p>3.0 mL from the gallic acid sample solution was filled into 50 mL volumetric falsk every 20 minutes, and measured 6 times according to the method of 2.1, RSD = 1.02%. It showed that the samples were in good stability within 120 minutes.</p><fig id="fig1"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref></label><caption><title> Standard curve of gallic acid</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/3-5500194x6.png"/></fig></sec><sec id="s3_5"><title>3.5. Reproducibility Test</title><p>Six pieces of P. chinense (2.0 g) was treated by water bath for extraction of gallic acid under the designed conditions. The experiment was repeated six times, and measured 6 times according to the method of 2.1, RSD = 1.34%. It showed that the repeatability of the method was good.</p></sec><sec id="s3_6"><title>3.6. Recovery Test</title><p>Six pieces of P. chinense (6.0 g) were weighed and added a certain amount of gallic acid standard, then measured absorbance values of gallic acid according to the method of 2.1. The experiment was repeated six times, and calculated the recovery of 98.0%, RSD = 1.42%. It showed that the recovery of the method was good. (see <xref ref-type="table" rid="table1">Table 1</xref> ).</p></sec><sec id="s3_7"><title>3.7. Single Factor Results</title><sec id="s3_7_1"><title>3.7.1. Effect of Solid/Liquid Ratio on Extraction Yield of Gallic Acid from P. chinense</title><p>In this work, the effect of solid/liquid ratio on extraction yield of gallic acid from P. chinense was investigated, and the results were listed in <xref ref-type="fig" rid="fig2">Figure 2</xref>. Firstly, the other extraction conditions of gallic acid from P. chinense, e.g. extraction temperature, extraction time and ethanol concentration, were fixed at 70˚C, 1 h, 60%, respectively and solid/liquid ratio was set at 1:10, 1:15, 1:20, 1:25, 1:30, 1:35. As be shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>, extraction yield of gallic acid from P. chinense continued to increase with solid/liquid ratio and reached the peak value (4.71%) when solid/liquid ratio was 1:25. The extraction yield of gallic acid from P. chinense started to decrease after solid/liquid ratio exceeded 1:25. Therefore, the solid/liquid ratio being set at 1:25 was appropriate.</p></sec><sec id="s3_7_2"><title>3.7.2. Effect of Ethanol Concentration on Extraction Yield of Gallic Acid from P. chinense</title><p>The effect of ethanol concentration on extraction yield of gallic acid from P. chinense was shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>. Firstly, ethanol concentration was set at 30%, 40%, 50%, 60%, 70%, and 80%, while other extraction parameters were given as followings: extraction temperature 70˚C, solid/liquid ratio 1:20 and extraction time 1 h. There was similar trend as above for varying solid/liquid ratio on extraction yield of gallic acid from P. chinense. With increasing the ethanol concentration from 30% to 70%, the extraction yield of gallic acid from P. chinense first increased and then decreased. The maximum was 4.78% when the ethanol concentration was 70% (see <xref ref-type="fig" rid="fig3">Figure 3</xref>). Therefore, the ethanol concentration being set at 70% was appropriate.</p></sec><sec id="s3_7_3"><title>3.7.3. Effect of Extraction Time on Extraction Yield of Gallic Acid from P. chinense</title><p>The effect of extraction time on extraction yield of gallic acid from P. chinense was shown in <xref ref-type="fig" rid="fig4">Figure 4</xref>. Firstly, extraction time was set at 1, 1.5, 2, 2.5, 3, 3.5 h, while other extraction parameters were given as followings: extraction temperature 70˚C, solid/liquid ratio 1:20 and ethanol concentration 60%. It could be found that with increase of extraction time from 1 to 1.5 h, the extraction yield of gallic acid from P. chinense increased gradually, and then increased slowly after 1.5 h. Taking everything into account, extraction time being set at 3 h was appropriate.</p><fig id="fig2"  position="float"><label><xref ref-type="fig" rid="fig2">Figure 2</xref></label><caption><title> The effect of solid-liquid ratio on extraction rate</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/3-5500194x7.png"/></fig><fig id="fig3"  position="float"><label><xref ref-type="fig" rid="fig3">Figure 3</xref></label><caption><title> The effect of ethanol concentration on extraction rate</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/3-5500194x8.png"/></fig><fig id="fig4"  position="float"><label><xref ref-type="fig" rid="fig4">Figure 4</xref></label><caption><title> The effect of extraction time on extraction rate</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/3-5500194x9.png"/></fig><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Result of recovery of gallic acid in Penthorum chinense Pursh</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >No</th><th align="center" valign="middle" >Original/mg</th><th align="center" valign="middle" >Added/mg</th><th align="center" valign="middle" >Detected/mg</th><th align="center" valign="middle" >Recovery/%</th><th align="center" valign="middle" >X/%</th><th align="center" valign="middle" >RSD/%</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2.7878</td><td align="center" valign="middle" >0.7260</td><td align="center" valign="middle" >3.500</td><td align="center" valign="middle" >98.2</td><td align="center" valign="middle" ></td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >2.7864</td><td align="center" valign="middle" >0.7075</td><td align="center" valign="middle" >3.478</td><td align="center" valign="middle" >97.9</td><td align="center" valign="middle" ></td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2.7841</td><td align="center" valign="middle" >0.7278</td><td align="center" valign="middle" >3.513</td><td align="center" valign="middle" >100.2</td><td align="center" valign="middle" ></td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >2.7856</td><td align="center" valign="middle" >0.7131</td><td align="center" valign="middle" >3.490</td><td align="center" valign="middle" >98.8</td><td align="center" valign="middle" >98.0</td><td align="center" valign="middle" >1.42</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >2.7834</td><td align="center" valign="middle" >0.7023</td><td align="center" valign="middle" >3.463</td><td align="center" valign="middle" >96.8</td><td align="center" valign="middle" ></td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >2.7822</td><td align="center" valign="middle" >0.7045</td><td align="center" valign="middle" >3.460</td><td align="center" valign="middle" >96.2</td><td align="center" valign="middle" ></td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap></sec><sec id="s3_7_4"><title>3.7.4. Effect of Extraction Temperature on Extraction Yield of Gallic acid from P. chinense</title><p>In this work, the effect of different extraction temperature on extraction yield of gallic acid from P. chinense was investigated, and the results were listed in <xref ref-type="fig" rid="fig5">Figure 5</xref>. Firstly, the other extraction conditions of gallic acid from P. chinense, e.g. solid/liquid ratio, extraction time and ethanol concentration, were fixed at 1:20, 1h, 60%, respectively and extraction temperature was set at 50˚C, 60˚C, 70˚C, 80˚C, 90˚C, 100˚C. As be shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>, extraction yield of gallic acid from P. chinense continued to increase as a whole with the increasing extraction temperature. It showed that effect of extraction temperature on extraction yield of gallic acid from P. chinense were stable. Due to the boiling point of solvent was close to 80˚C, the extraction temperature being set at 80˚C was appropriate.</p></sec></sec><sec id="s3_8"><title>3.8. Optimization of the Extraction Parameters of Gallic Acid from P. chinense</title><p>The first step in the extraction parameters of gallic acid from P. chinense was to optimize the operating conditions to obtain an efficient extraction of the target compounds. Since various parameters potentially affected the extraction process, the optimization of the experimental conditions was a critical step in the development of a solvent extraction method. In fact, the extraction temperature, extraction time, solid/liquid ratio and ethanol concentration were generally considered to be the most important factors. Optimization of the suitable extraction conditions in the gallic acid extraction could be carried out by using an experimental design. In the present study, all selected factors were examined using an orthogonal L<sub>9</sub> (3<sup>4</sup>) test design. The total evaluation index was used to analysis by statistical method. Factors and levels are presented in <xref ref-type="table" rid="table2">Table 2</xref>. The results of orthogonal test were presented in <xref ref-type="table" rid="table3">Table 3</xref>. Analysis of variance was presented in <xref ref-type="table" rid="table4">Table 4</xref>.</p><p>The results of experiments presented in <xref ref-type="table" rid="table3">Table 3</xref> indicated that the maximum extraction yield of gallic acid was 5.21%. However, we couldn’t select the best extraction conditions only based on these outcomes in <xref ref-type="table" rid="table3">Table 3</xref>, and a further orthogonal analysis was warranted. Thus, the K and R values were calculated and listed in <xref ref-type="table" rid="table3">Table 3</xref>. As seen from <xref ref-type="table" rid="table3">Table 3</xref>, we could find that the influence to the mean extraction yields of the compounds decreased in the order: A &gt; C = B &gt; D according to the R values. The ethanol concentration was found to be the most important determinant of the yield. In other words, the yield of the gallic acid was obtained when extraction temperature, extraction time, solid/liquid ratio and ethanol concentration were 90˚C, 2.5 h, 1:30 and 60%, respectively. According to Analysis of variance, ethanol concentration was significant in determining a higher extraction yield (<xref ref-type="table" rid="table4">Table 4</xref>). There were non-significant interaction effects between all other factors.</p></sec><sec id="s3_9"><title>3.9. The Best Process Validation Test</title><p>Under the condition of the optimization process, the experiment was repeated six times, and measured the average yield of gallic acid of 4.85%, RSD = 1.02%. It showed that the process was stable.</p></sec></sec><sec id="s4"><title>4. Results and Discussion</title><p>Chen [<xref ref-type="bibr" rid="scirp.55816-ref3">3</xref>] reported that four extraction methods of gallic acid were compared by orthogonal test, such as water bath, ultrasonic water bath, decoction, percolation. It determined the optimum condition that extraction temperature, extraction speed, solid/liquid ratio and ethanol concentration were 90˚C, 3 seconds at the rate of 1 drop,</p><fig id="fig5"  position="float"><label><xref ref-type="fig" rid="fig5">Figure 5</xref></label><caption><title> The effect of temperature on extraction rate</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/3-5500194x10.png"/></fig><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Factors and levels of orthogonal test</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Levels</th><th align="center" valign="middle" >Ethanol concentration (%)</th><th align="center" valign="middle" >Solid/liquid ratio</th><th align="center" valign="middle" >Extraction time (h)</th><th align="center" valign="middle" >Extraction temperature (˚C)</th></tr></thead><tr><td align="center" valign="middle" ></td><td align="center" valign="middle" >A</td><td align="center" valign="middle" >B</td><td align="center" valign="middle" >C</td><td align="center" valign="middle" >D</td></tr><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >60%</td><td align="center" valign="middle" >1:20</td><td align="center" valign="middle" >2.5</td><td align="center" valign="middle" >70</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >70%</td><td align="center" valign="middle" >1:25</td><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >80</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >80%</td><td align="center" valign="middle" >1:30</td><td align="center" valign="middle" >3.5</td><td align="center" valign="middle" >90</td></tr></tbody></table></table-wrap><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Results of L<sub>9</sub>(3<sup>4</sup>) orthogonal test</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Levels</th><th align="center" valign="middle" >A</th><th align="center" valign="middle" >B</th><th align="center" valign="middle" >C</th><th align="center" valign="middle" >D</th><th align="center" valign="middle" >Extraction efficiency (%)</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >5.16</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >5.01</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >5.21</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >5.15</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >4.76</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >5.20</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >4.40</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >4.47</td></tr><tr><td align="center" valign="middle" >9</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >4.67</td></tr><tr><td align="center" valign="middle" >I</td><td align="center" valign="middle" >15.38</td><td align="center" valign="middle" >14.63</td><td align="center" valign="middle" >14.83</td><td align="center" valign="middle" >14.59</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >II</td><td align="center" valign="middle" >15.11</td><td align="center" valign="middle" >14.71</td><td align="center" valign="middle" >14.83</td><td align="center" valign="middle" >14.61</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >III</td><td align="center" valign="middle" >13.54</td><td align="center" valign="middle" >15.08</td><td align="center" valign="middle" >14.37</td><td align="center" valign="middle" >14.83</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >R</td><td align="center" valign="middle" >1.84</td><td align="center" valign="middle" >0.45</td><td align="center" valign="middle" >0.46</td><td align="center" valign="middle" >0.24</td><td align="center" valign="middle" >-</td></tr></tbody></table></table-wrap><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Analysis of variance</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Factors</th><th align="center" valign="middle" >Sum of squares</th><th align="center" valign="middle" >F</th><th align="center" valign="middle" >F value</th><th align="center" valign="middle" >F critical value</th><th align="center" valign="middle" >Significant</th></tr></thead><tr><td align="center" valign="middle" >A</td><td align="center" valign="middle" >0.674</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >44.636</td><td align="center" valign="middle" >19</td><td align="center" valign="middle" ><sup>** </sup></td></tr><tr><td align="center" valign="middle" >B</td><td align="center" valign="middle" >0.059</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3.9072</td><td align="center" valign="middle" >19</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >C</td><td align="center" valign="middle" >0.083</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >5.5333</td><td align="center" valign="middle" >19</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >D</td><td align="center" valign="middle" >0.011</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >0.7285</td><td align="center" valign="middle" >19</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p>Note: F(0.1) = 9, F(0.05) = 19.</p><p>1:30 and 60%, respectively. Four methods had their advantages and disadvantages, but the percolation method consumed time longer, was not suitable for the manufacturing. So gallic acid from Penthorum chinense pursh extracted with aqueous ethanol was studied. With extraction amount of gallic acid as index, based on single factor analysis, influence of solid/liquid ratio, ethanol concentration, fetch time and extraction temperature on extraction technology were investigated by orthogonal test. The yield of the gallic acid of 4.85% was obtained when extraction temperature, extraction time, solid/liquid ratio and ethanol concentration were 90˚C, 2.5 h, 1:30 and 60%, respectively. In this experiment, the aqueous ethanol extraction could shorten extracting time, was more suitable for the industrial production. In the experiment, gallic acid content was determined by simple and fast UV. The method was suitable for quality control in actual manufacturing, and precision, stability, repeatability was good.</p></sec><sec id="s5"><title>Acknowledgements</title><p>This work was supported by the Fund of Doctor’s Program in Chongqing Normal University (12XLB006) and the Open Program of Engineering Research Center of Biotechnology of Active Materials (Ministry of Education) in Chongqing Normal University.</p><p>In this experiment, our work got these teachers’ help (He Daiping, Xiao Feng), thanks!</p></sec><sec id="s6"><title>NOTES</title></sec></body><back><ref-list><title>References</title><ref id="scirp.55816-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Xiang, H., Yang, J., Fu, X., et al. (2013) Optimization of Extraction Technology of Penthorum chinense by Orthogonal Test. 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