<?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">OALibJ</journal-id><journal-title-group><journal-title>Open Access Library Journal</journal-title></journal-title-group><issn pub-type="epub">2333-9705</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/oalib.1104090</article-id><article-id pub-id-type="publisher-id">OALibJ-80298</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Biomedical&amp;Life Sciences</subject><subject> Business&amp;Economics</subject><subject> Chemistry&amp;Materials Science</subject><subject> Computer Science&amp;Communications</subject><subject> Earth&amp;Environmental Sciences</subject><subject> Engineering</subject><subject> Medicine&amp;Healthcare</subject><subject> Physics&amp;Mathematics</subject><subject> Social Sciences&amp;Humanities</subject></subj-group></article-categories><title-group><article-title>
 
 
  Degradation Characteristics of Oil Degrading &lt;i&gt;Candida tropicalis&lt;/i&gt;
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Ya-Bin</surname><given-names>Zhan</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Fang-Min</surname><given-names>Li</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-Chu</surname><given-names>Yu</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>Tao</surname><given-names>Jiang</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Li-An</surname><given-names>Ma</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff3"><addr-line>College of Animal Science, Yangtze University, Jingzhou, China</addr-line></aff><aff id="aff1"><addr-line>College of Life Science, Yangtze University, Jingzhou, China</addr-line></aff><aff id="aff2"><addr-line>College of Chemical and Environmental Engineering, Yangtze University, Jingzhou, China</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>1766784675@qq.com(YZ)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>01</day><month>11</month><year>2017</year></pub-date><volume>04</volume><issue>11</issue><fpage>1</fpage><lpage>10</lpage><history><date date-type="received"><day>30,</day>	<month>October</month>	<year>2017</year></date><date date-type="rev-recd"><day>11,</day>	<month>November</month>	<year>2017</year>	</date><date date-type="accepted"><day>14,</day>	<month>November</month>	<year>2017</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>
 
 
  Objective: The aim of study is to research the degradation characteristics of oil degrading 
  Candida tropicalis
   (G-94). Methods: Effects of temperature, pH, oil concentration, salt concentration, inoculation amount, N and P source on the oil removal rate of G-94 were studied by single factor test. Meanwhile, the effects of temperature, pH, oil concentration and salt concentration on the oil removal rate of G-94 were optimized by
   orthogonal design. Result: The orthogonal design showed that the oil removal rate of G-94 could reach 25.83%, 28.56% and 30.90% at 10 d, 20 d and 40 d under the optimal conditions which was 25℃, initial pH 8.0, oil concentration 1.0%, salt concentration 0.4%, inoculum amount 4%, the optimal N and P were (NH
  <sub style="text-align:justify;white-space:normal;">4</sub>
  )
  <sub style="text-align:justify;white-space:normal;">2</sub>
  SO
  <sub style="text-align:justify;white-space:normal;">4</sub>
   and K
  <sub style="text-align:justify;white-space:normal;">2</sub>
  HPO
  <sub style="text-align:justify;white-space:normal;">4</sub>
  . Conclusion: This experiment studied the degradation characteristics of G-94, which paved the way for the remediation of petroleum contaminated soil.
 
</p></abstract><kwd-group><kwd>Degrading Yeast</kwd><kwd> &lt;i&gt;Candida tropicalis&lt;/i&gt;</kwd><kwd> Oil Degrading</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Oil contains many highly concentrated toxic materials, and oil contamination can negatively influence soil microbes and plants, as well as contaminate groundwater, which may be used for drinking or agriculture [<xref ref-type="bibr" rid="scirp.80298-ref1">1</xref>] . To eliminate these pollution compounds, processes have been developed based on physicochemical techniques, including the vacuum extraction of hydrocarbons, soil washing, electrokinetic incineration and recovery using solvents [<xref ref-type="bibr" rid="scirp.80298-ref2">2</xref>] . However, these methods produce toxic remnants that need to be decontaminated, which involve a high economic cost that is an obstacle to implementation [<xref ref-type="bibr" rid="scirp.80298-ref3">3</xref>] [<xref ref-type="bibr" rid="scirp.80298-ref4">4</xref>] . Fortunately, bioremediation is the microbial degradation of organic pollutants such as petroleum in soil and groundwater. This technique has the benefits of high treatment efficiency, low cost, relatively quick action, in site and ex site application, and compatibility with other techniques [<xref ref-type="bibr" rid="scirp.80298-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.80298-ref6">6</xref>] [<xref ref-type="bibr" rid="scirp.80298-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.80298-ref8">8</xref>] .</p><p>Thus, in order to get insight of the bioremediation process of hydrocarbon in Qianjiang Guanghua Oilfield, the present study focused on degradation characteristics of indigenous hydrocarbon-degrading Candida tropicalis (G-94) with regards to the conditions for optimizing their activities and the efficient cleanup of the hydrocarbon pollutants.</p></sec><sec id="s2"><title>2. Materials and Methods</title><sec id="s2_1"><title>2.1. Source of Isolation</title><p>The G-94 was isolated from Qianjiang Guanghua Oilfield on June 2015, stored in the laboratory of College of Life Science, Yangtze University [<xref ref-type="bibr" rid="scirp.80298-ref9">9</xref>] .</p></sec><sec id="s2_2"><title>2.2. Growth Study</title><p>Experiments were conducted in the oil medium described above with 0.5% oil (w/v) as sole carbon and energy source. Growth was monitored by measuring optical density at 420 nm with a TU-1900 spectrophotometer [<xref ref-type="bibr" rid="scirp.80298-ref10">10</xref>] .</p></sec><sec id="s2_3"><title>2.3. Determination of Oil Removal Rate</title><p>The oil removal rate was determined by gravimetric method [<xref ref-type="bibr" rid="scirp.80298-ref10">10</xref>] . A total of 80 ml methylene chloride was added to the oil triangle bottle to extract the oil. The water in the oil was dried at room temperature until the anhydrous sodium sulfate column was removed, until the organic solvent completely evaporated. Place the oil in the vacuum drying box at 40˚C and keep the vacuum at 0.04 Mpa for 30 min. Then remove it and leave it in the dryer for 30 min and to weigh. The oil removal rate is calculated according to the formula (1):</p><p>D = ( C 0 − C S ) C 0 &#215; 100 % (1)</p><p>D: The oil removal rate, %; C<sub>0</sub>: blank hydrocarbon concentration, mg/L; CS: concentration of petroleum hydrocarbon in the culture fluid, mg/L [<xref ref-type="bibr" rid="scirp.80298-ref10">10</xref>] .</p></sec><sec id="s2_4"><title>2.4. Study on Degradation Characteristics</title><sec id="s2_4_1"><title>2.4.1. Single Factor Test</title><p>The yeast was inoculated into potato sucrose liquid medium. The yeast were inoculated in logarithmic phase, centrifuged, removed supernatant, washed with sterile normal saline, and adjusted to OD<sub>420</sub> = 9.185. In the basic culture medium at the same time, by changing the growth conditions in different temperature, pH, oil concentration, salt concentration, inoculation amount, N source, P source on a horizontal shaker (150 rpm) at 35˚C in 100 ml oil medium for 5 d. Learning the suitable growth conditions of G-94 by the determination of biomass (OD<sub>420</sub>).</p></sec><sec id="s2_4_2"><title>2.4.2. Orthogonal Test</title><p>Four factors and 3 levels orthogonal test (<xref ref-type="table" rid="table1">Table 1</xref>) was carried out with temperature, pH, oil concentration and salt concentration. With 4% inoculation on a horizontal shaker (150 rpm) in 100 ml oil medium for 5 d. Learning the optimum growth condition of G-94 by the determination of biomass (OD<sub>420</sub>).</p></sec><sec id="s2_4_3"><title>2.4.3. Verification Test</title><p>Under orthogonal optimum conditions, the oil removal rate of G-94 was measured at 10, 20 and 40 day, respectively.</p></sec><sec id="s2_4_4"><title>2.4.4. Statistic Analysis</title><p>SAS software was used to test the significance difference (P &lt; 0.05) and extremely significant difference (P &lt; 0.01).</p></sec></sec><sec id="s2_5"><title>2.5. Determination of Growth Curve</title><p>Under the optimum conditions, the strain of G-94 was injected into the oil medium with 4% inoculum, drawing the growth curve by measuring its OD<sub>420</sub>.</p></sec></sec><sec id="s3"><title>3. Results and Analysis</title><sec id="s3_1"><title>3.1. Physiology</title><sec id="s3_1_1"><title>3.1.1. Single Factor Test</title><p>1) Temperature</p><p>The biomass of G-94 was effected by temperature as shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>. The biomass decreased with the increase of temperature. There were larger biomass of G-94, when the temperature were 25˚C (OD<sub>420</sub> = 1.622) and 30˚C (OD<sub>420</sub> = 1.537). Compared with other treatments, there were significant differences.</p><p>Extremely significant difference (P &lt; 0.01); Significance difference (P &lt; 0.05). Same as below.</p><p>2) pH</p><p>The biomass of G-94 was effected by pH as shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>. The biomass increased firstly and decreased lastly with the increase of pH. There was larger biomass of G-94, when the pH was 7.5 (OD<sub>420</sub> = 0.960), 8.0 (OD<sub>420</sub> = 1.183) and 9.0 (OD<sub>420</sub> = 0.991). Compared with other treatments, there were extremely significant differences.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Factor levels table</title></caption><table><tbody><thead><tr><th align="center" valign="middle" ></th><th align="center" valign="middle" >A (˚C)</th><th align="center" valign="middle" >B</th><th align="center" valign="middle" >C (%)</th><th align="center" valign="middle" >D (%)</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >25</td><td align="center" valign="middle" >7.8</td><td align="center" valign="middle" >0.1</td><td align="center" valign="middle" >0.3</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >28</td><td align="center" valign="middle" >8.0</td><td align="center" valign="middle" >0.2</td><td align="center" valign="middle" >0.4</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >30</td><td align="center" valign="middle" >8.2</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >0.5</td></tr></tbody></table></table-wrap><p>A: Temperature; B: pH; C: oil concentration; D: salt concentration.</p><p>3) Oil concentration</p><p>The biomass of G-94 was effected by oil concentration as shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>. There were larger biomass of G-94, when the oil concentration were 1.0% (OD<sub>420</sub> = 1.150). Compared with the biomass of oil concentrate 0.2%, 0.4%, 0.6% and 0.8%, there were no significant differences.</p><p>4) Salinity</p><p>The biomass of G-94 was effected by salt concentration as shown in <xref ref-type="fig" rid="fig4">Figure 4</xref>. The biomass increased firstly and decreased lastly with the increase of salt concentration. There were larger biomass of G-94, when the salt concentration was 0.4% (OD<sub>420</sub> = 1.722). Compared with other treatments, there were extremely significant differences.</p><p>5) Inoculation amount</p><p>The biomass of G-94 was effected by inoculation amount as shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>. The biomass increased with the increase of inoculation amount. There was larger biomass of G-94, when the inoculation amount were 4% (OD<sub>420</sub> = 1.739). Compared with other treatments, there were no extremely significant differences.</p><p>6) Nitrogen</p><p>The biomass of G-94 was effected by nitrogen source as shown in <xref ref-type="fig" rid="fig6">Figure 6</xref>. There were larger biomass of G-94, when the nitrogen source were (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> (OD<sub>420</sub> = 0.593), NH<sub>4</sub>NO<sub>3</sub> (OD<sub>420</sub> = 1.314) and NH<sub>4</sub>NO<sub>3</sub> (OD<sub>420</sub> = 1.175). Compared with the biomass of NH<sub>4</sub>Cl and KNO<sub>3</sub>, there were extremely significant differences.</p><p>7) Phosphorus</p><p>The biomass of G-94 was effected by phosphorus source as shown in <xref ref-type="fig" rid="fig7">Figure 7</xref>. There were larger biomass of G-94, when the phosphorus source were K<sub>2</sub>HPO<sub>4</sub> (OD<sub>420</sub> = 1.356). Compared with the biomass of K<sub>2</sub>HPO<sub>4</sub>, Na<sub>2</sub>HPO<sub>4</sub> and NaH<sub>2</sub>PO<sub>4</sub>, there were extremely significant differences.</p></sec><sec id="s3_1_2"><title>3.1.2. Orthogonal Test</title><p>Different conditions had obvious influence on the oil removal rate of G-94. The maximum range of temperature is the key factor affecting the oil removal rate of</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> The orthogonal design and analysis of G-94</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Treatment</th><th align="center" valign="middle" >A (˚C)</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" >Result</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >25</td><td align="center" valign="middle" >7.8</td><td align="center" valign="middle" >0.1</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >1.197</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >25</td><td align="center" valign="middle" >8.0</td><td align="center" valign="middle" >0.2</td><td align="center" valign="middle" >0.4</td><td align="center" valign="middle" >1.183</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >25</td><td align="center" valign="middle" >8.2</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >0.5</td><td align="center" valign="middle" >1.544</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >28</td><td align="center" valign="middle" >7.8</td><td align="center" valign="middle" >0.2</td><td align="center" valign="middle" >0.5</td><td align="center" valign="middle" >1.468</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >28</td><td align="center" valign="middle" >8.0</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >1.589</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >28</td><td align="center" valign="middle" >8.2</td><td align="center" valign="middle" >0.1</td><td align="center" valign="middle" >0.4</td><td align="center" valign="middle" >1.025</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >30</td><td align="center" valign="middle" >7.8</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >0.4</td><td align="center" valign="middle" >1.537</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >30</td><td align="center" valign="middle" >8.0</td><td align="center" valign="middle" >0.1</td><td align="center" valign="middle" >0.5</td><td align="center" valign="middle" >1.066</td></tr><tr><td align="center" valign="middle" >9</td><td align="center" valign="middle" >30</td><td align="center" valign="middle" >8.2</td><td align="center" valign="middle" >0.2</td><td align="center" valign="middle" >0.3</td><td align="center" valign="middle" >1.264</td></tr><tr><td align="center" valign="middle" >K1</td><td align="center" valign="middle" >1.308</td><td align="center" valign="middle" >1.401</td><td align="center" valign="middle" >1.096</td><td align="center" valign="middle" >1.350</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >K2</td><td align="center" valign="middle" >1.361</td><td align="center" valign="middle" >1.279</td><td align="center" valign="middle" >1.305</td><td align="center" valign="middle" >1.248</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >K3</td><td align="center" valign="middle" >1.289</td><td align="center" valign="middle" >1.278</td><td align="center" valign="middle" >1.557</td><td align="center" valign="middle" >1.359</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >R</td><td align="center" valign="middle" >0.072</td><td align="center" valign="middle" >0.123</td><td align="center" valign="middle" >0.467</td><td align="center" valign="middle" >0.111</td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p>A: Temperature; B: pH; C: oil concentration; D: salt concentration.</p><p>G-94, followed by pH and oil concentration, while salt concentration has the least influence. Therefore, the suitable condition of oil removal rate of G-94 was A<sub>2</sub>B<sub>1</sub>C<sub>3</sub>D<sub>3</sub> which was 28˚C, pH 7.8, oil concentration 0.3%, salt concentration 0.5% (<xref ref-type="table" rid="table2">Table 2</xref>).</p></sec><sec id="s3_1_3"><title>3.1.3. Verification Test</title><p>The results of Verification test were shown in <xref ref-type="fig" rid="fig8">Figure 8</xref>. Under orthogonal optimum conditions, the oil removal rate of G-94 reached to 25.83%, 28.56% and 30.90% at 10, 20 and 40 day, respectively.</p></sec></sec><sec id="s3_2"><title>3.2. Determination of Growth Curve</title><p>The result of determination of growth curve was shown in <xref ref-type="fig" rid="fig9">Figure 9</xref>. The 0 - 0.5 day was the lag phase of G-94; In this period, the reason why no biomass increase is that bacteria were first introduced into a fresh media. The 0.5 - 4 day was the exponential of G-94; In this period, the strain rapidly propagated and gradually turned the oil medium to muddy. The 4.5 - 13 day was the stationary phase of G-94; In this period, death rate = rate of reproduction of G-94 and continues for a long time.</p></sec></sec><sec id="s4"><title>4. Discussion and Conclusion</title><sec id="s4_1"><title>4.1. Discussion</title><p>The optimal oil removal condition of G-94 was determined through biomass of petroleum degradation microorganism, not the oil removal rate. The reason why we use the biomass is that biomass is positively correlated with degradation rate and it is more convenient than oil removal rate [<xref ref-type="bibr" rid="scirp.80298-ref10">10</xref>] .</p><p>Candida tropicalis used to repair potato starch wastewater [<xref ref-type="bibr" rid="scirp.80298-ref11">11</xref>] , produce xylitol [<xref ref-type="bibr" rid="scirp.80298-ref12">12</xref>] and Long Chain Dicarboxylic Acid [<xref ref-type="bibr" rid="scirp.80298-ref13">13</xref>] . There were few reports about Candida tropicalis degrading oil.</p><p>A strain of G-94 with petroleum as the sole carbon source was isolated from</p><p>the soil contaminated by petroleum for a long time. The effects of temperature, pH, oil concentration, salt concentration, inoculum amount, N and P source on the degradation of oil were studied. Different conditions had great influences on the oil removal rate of G-94. The G-94 has larger biomass when the inoculation amount was 4% (OD<sub>420</sub> = 1.739); Finally, the inoculation amount 4% was used to do the orthogonal experiment. The optimum N and P source was (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> and K<sub>2</sub>HPO<sub>4</sub>, which is basically consistent with the oil medium. Therefore, the temperature, pH and oil concentration and salt concentration were selected to do orthogonal test to further study the optimum conditions for degrading oil.</p><p>The oil removal rate of G-94 reached to 25.83% on 10<sup>th</sup> day. The oil removal rate of G-94 reached 28.56% on 20<sup>th</sup> day, increased by 10.57% compared with 10<sup>th</sup> day. The oil removal rate of G-94 reached 30.90% on 40<sup>th</sup> day, increased by 8.19% compared with 20<sup>th</sup> day. Maybe, the nutrition in the bottle had been consumed with the passage of time, so as to the oil removal rate of increase was not obvious. In order to improve the oil removal rate, nutrition can be added to the bottle; meanwhile, fresh mineral salt liquid media need to be replaced, because degradation of petroleum products by G-94 may be toxic.</p><p>Oil degradation is limited by many factors in the soil [<xref ref-type="bibr" rid="scirp.80298-ref14">14</xref>] [<xref ref-type="bibr" rid="scirp.80298-ref15">15</xref>] . The development and utilization of the genetic resources of G-94 for petroleum degradation and their application in the remediation of petroleum contaminated soils should be further studied.</p></sec><sec id="s4_2"><title>4.2. Conclusion</title><p>The optimal conditions of oil removal rate of G-94 were 28˚C, pH 7.8, oil concentration 0.3%, salt concentration 0.5%, inoculation amount 4%, N and P was (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> and K<sub>2</sub>HPO<sub>4</sub>. Under orthogonal optimum conditions, the oil removal rate of G-94 reached to 25.83%, 28.56% and 30.90% on the 10<sup>th</sup>, 20<sup>th</sup> and 40<sup>th</sup> day, respectively.</p></sec></sec><sec id="s5"><title>Cite this paper</title><p>Zhan, Y.-B., Li, F.-M., Yu, W.-C., Jiang, T. and Ma, L.-A. (2017) Degradation Characteristics of Oil Degrading Candida tropicalis. Open Access Library Journal, 4: e4090. https://doi.org/10.4236/oalib.1104090</p></sec></body><back><ref-list><title>References</title><ref id="scirp.80298-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Hong, J.H., Kim, J., Choi, O.K., Cho, K.S. and Ryu, H.W. (1997) Characterization of A Diesel-Degrading Bacterium, Pseudomonas Aeruginosa IU5, Isolated from Oil-Contaminated Soil in Korea. 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