<?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">OJMS</journal-id><journal-title-group><journal-title>Open Journal of Marine Science</journal-title></journal-title-group><issn pub-type="epub">2161-7384</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ojms.2018.82015</article-id><article-id pub-id-type="publisher-id">OJMS-83988</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>
 
 
  An Effective Extract Method of Phospholipids from Antarctic Krill &lt;em&gt;Euphausea superba&lt;/em&gt;
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Xiaoqing</surname><given-names>Tian</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>Chengqi</surname><given-names>Fan</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>Zhidong</surname><given-names>Liu</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>Hongliang</surname><given-names>Huang</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>Yanan</surname><given-names>Lu</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff3"><addr-line>Key Laboratory of Oceanic and Polar Fisheries, Ministry of Agriculture, Shanghai, China</addr-line></aff><aff id="aff2"><addr-line>East China Sea Fisheries Research Institute, Chinese Academy of Fishery Sciences, Shanghai, China</addr-line></aff><aff id="aff1"><addr-line>Key Laboratory of East China Sea Fishery Resources Exploitation, Ministry of Agriculture, Shanghai, China</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>luyn@ecsf.ac.cn(YL)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>11</day><month>02</month><year>2018</year></pub-date><volume>08</volume><issue>02</issue><fpage>293</fpage><lpage>299</lpage><history><date date-type="received"><day>8,</day>	<month>February</month>	<year>2018</year></date><date date-type="rev-recd"><day>22,</day>	<month>April</month>	<year>2018</year>	</date><date date-type="accepted"><day>25,</day>	<month>April</month>	<year>2018</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>
 
 
  
    Phospholipids are one of the major bioactive ingredients of Antarctic krill 
   <em>Euphausea superba</em>. A feasible and effective extraction method of Antarctic krill oil was investigated and modified by orthogonal test which the ratio of solid to liquid was 1:2.5, extraction time was 5 min, ratio of ethyl acetate (EA) and n-butanol (BuOH) was 1:1. With this method, the extract of krill oil has a higher phospholipids content of 27.7% - 42.3%, together with total oil yields of 4.15% - 6.18%. 
  
 
</p></abstract><kwd-group><kwd>Phospholipids</kwd><kwd> Antarctic Krill</kwd><kwd> &lt;em&gt;Euphausea superba&lt;/em&gt;</kwd><kwd> Extraction</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Phospholipids are not only a kind of important bioactive ingredients, but also essential nutrients in the metabolism of organisms. They were used in food, medicine, and industry widely [<xref ref-type="bibr" rid="scirp.83988-ref1">1</xref>] [<xref ref-type="bibr" rid="scirp.83988-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.83988-ref3">3</xref>] . At present, there were many preparation and purification methods of phospholipids, such as solvent extraction, supercritical fluid extraction, and column chromatography, as well as analytic methods including thin layer chromatography (TLC), high performance liquid chromatography (HPLC), and nuclear magnetic resonance (NMR) [<xref ref-type="bibr" rid="scirp.83988-ref4">4</xref>] . Although the advanced phospholipid production technology has been applied in Europe, America, Japan and some other countries, it is still not popular in China.</p><p>According to the abundance phospholipids, Euphausea superba (<xref ref-type="fig" rid="fig1">Figure 1</xref>), one major species of Antarctic krill, is a biological enrichment library of phospholipids [<xref ref-type="bibr" rid="scirp.83988-ref3">3</xref>] . The main components of the phospholipids in Antarctic krill are phosphatidyl choline (PC), phosphatidyl ethanolamine (PE), phosphatidyl</p><p>inositol (PI) and so on [<xref ref-type="bibr" rid="scirp.83988-ref5">5</xref>] .</p><p>In our continuous investigation on feasible and effective extraction method of Antarctic krill oil, an improved solvent extraction and HPLC were used for extraction and detection of the phospholipid from E. superba. The high content phospholipid was therefore obtained.</p></sec><sec id="s2"><title>2. Experimental Section</title><sec id="s2_1"><title>2.1. General Procedures</title><p>Homogenizer (DJ126-DEG1) was offered by Guangdong Midea boutique electrical appliance manufacturing co., LTD. Centrifugal machine(KUBOTA 7780) was obtained from Beijing dongxuntiandi medical instrument co. LTD. Agilent 1260 HPLC was used with the column of Atlantis HILIC Silica (4.6 &#215; 150 mm, 5 &#181;m). The ultraviolet spectrophotometer (752N) was purchased from Shanghai Precision and Scientific Instrument Corporation. L-α-phosphatidylcholine (P3556, ≥99%) and L-α-phosphatidylethanolamine (P7943, ≥97%) were obtained from Sigma. Astaxanthin was obtained from Dr. Ehrenstorfer GmbH. Methanol, acetonitrile and formic acid were chromatographic grade and obtained from J. C. Baker. Other reagents were analytical grade and obtained from Sinopharm chemical reagent Shanghai co., LTD.</p></sec><sec id="s2_2"><title>2.2. Biological Source</title><p>E. superb were collected from the 30th Chinese Antarctic scientific expedition, and was identified by Prof. Hong-Liang Huang. The samples were flushed with plenty of water and then kept frozen at −18˚C before use.</p></sec><sec id="s2_3"><title>2.3. Extraction</title><p>For better extraction of fat-soluble constituents, a solvent mixture of ethyl acetate (EA) and n-butanol (BuOH) was found to give a higher phospholipids content [<xref ref-type="bibr" rid="scirp.83988-ref6">6</xref>] . Then an orthogonal table of 3 factors and 3 levels is adopted in the design referred to Jian-Tong Zhang [<xref ref-type="bibr" rid="scirp.83988-ref7">7</xref>] . The ratio of solid to liquid, extraction time and ratio of solvent (EA/BuOH) were selected as the influencing factors, using the screening test to optimize the extraction process (<xref ref-type="table" rid="table1">Table 1</xref>).</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Factors and levels of orthogonal test</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Factor</th><th align="center" valign="middle"  colspan="3"  >level</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td></tr><tr><td align="center" valign="middle" >Ratio of solid to liquid (A)</td><td align="center" valign="middle" >1:1.5</td><td align="center" valign="middle" >1:2</td><td align="center" valign="middle" >1:2.5</td></tr><tr><td align="center" valign="middle" >Extraction time (B)/min</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >8</td></tr><tr><td align="center" valign="middle" >Ratio of solvent (C)</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >4:1</td></tr></tbody></table></table-wrap><p>The samples of E. superba were thus divided into 9 groups, and each group was 400 g. Every group was repeatedly extracted in homogenizer with ethyl acetate/n-butanol mixed solvent for 3 times at room temperature. Then the supernatants were combined and the solvent was removed in a rotary evaporator at 50˚C, then the fat-soluble extracts, namely krill oils, were obtained and weighed. The yields were calculated as in</p><p>Yields = weightofextract   ( g ) / wetweightof   E .   s u p e r b a   ( g ) (1)</p></sec><sec id="s2_4"><title>2.4. HPLC Analysis of Phospholipids</title><p>The standard solutions of L-α-phosphatidylethanolamine and L-α-phosphatidylcho-line in methanol were made up in two series of concentrations (0.2, 0.4, 0.6, 1.0, 1.4, 1.8 mg/mL and 0.06, 0.2, 0.4, 0.8, 1.2, 1.6, 2.0 mg/mL), respectively. Krill oil samples (2.0 mg) were dissolved in methanol to 1.0 mg/mL concentration, respectively. Each reference and sample solutions was filtrated with 0.45 &#181;m filter before injection to HPLC. The mobile phase was acetonitrile/ethanol/water containing 1% acetic acid (V:V:V = 30:69:1), with flow rate of 1.0 mL/min. The detection wavelength was 206 nm. The column temperature was room temperature and the injection volume was 10 uL.</p></sec><sec id="s2_5"><title>2.5. Analysis of Astaxanthin</title><p>Astaxanthin standard (0.12 mg) was dissolved with chloroform and made up as 10.0 mL parent solution. Then it was gradually diluted to give a series of solutions of 0.12, 0.6, 1.2, 6, 12 &#181;g/ml. Krill oil samples (20 mg) which was got from orthogonal test were dissolved in chloroform with concentration of 2 mg/mL. Each solution was tested in UV spectrophotometer under 478 nm with chloroform as blank control.</p><p>All statistical analyses were executed by using the Origin 9.1 software.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. The Yields of Krill Oils</title><p>Orthogonal test design is a scientific method of arranging and analyzing multifactor experiments. The main advantage of the orthogonal test design is that it can significantly reduce the number of trials, but it still covers all the possible tests [<xref ref-type="bibr" rid="scirp.83988-ref8">8</xref>] . The result of extraction yields was shown in <xref ref-type="table" rid="table2">Table 2</xref>. Firstly, fat soluble ingredients from E. superba accounted for 4.15% - 6.18%. They were in accord</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> The extraction yield of fat soluble ingredients from E. superba</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >No.</th><th align="center" valign="middle" >A</th><th align="center" valign="middle" >B (min)</th><th align="center" valign="middle" >C (EA/BuOH)</th><th align="center" valign="middle" >Ratio (%)</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1:1.5</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >4.68</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1:1.5</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >4.55</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >1:1.5</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >4:1</td><td align="center" valign="middle" >4.15</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >1:2</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >4.60</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >1:2</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >4:1</td><td align="center" valign="middle" >5.45</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >1:2</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >5.25</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >1:2.5</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >4:1</td><td align="center" valign="middle" >5.15</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >1:2.5</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >1:1</td><td align="center" valign="middle" >6.18</td></tr><tr><td align="center" valign="middle" >9</td><td align="center" valign="middle" >1:2.5</td><td align="center" valign="middle" >8</td><td align="center" valign="middle" >2:1</td><td align="center" valign="middle" >5.25</td></tr><tr><td align="center" valign="middle" >K1</td><td align="center" valign="middle" >13.38</td><td align="center" valign="middle" >14.43</td><td align="center" valign="middle" >16.10</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >K2</td><td align="center" valign="middle" >15.30</td><td align="center" valign="middle" >16.18</td><td align="center" valign="middle" >14.40</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >K3</td><td align="center" valign="middle" >16.58</td><td align="center" valign="middle" >14.65</td><td align="center" valign="middle" >14.75</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >κ1</td><td align="center" valign="middle" >4.46</td><td align="center" valign="middle" >4.81</td><td align="center" valign="middle" >5.37</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >κ2</td><td align="center" valign="middle" >5.10</td><td align="center" valign="middle" >5.39</td><td align="center" valign="middle" >4.80</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >κ3</td><td align="center" valign="middle" >5.53</td><td align="center" valign="middle" >4.88</td><td align="center" valign="middle" >4.92</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >R</td><td align="center" valign="middle" >1.07</td><td align="center" valign="middle" >0.58</td><td align="center" valign="middle" >0.57</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >The optimal level</td><td align="center" valign="middle" >A<sub>3</sub></td><td align="center" valign="middle" >B<sub>2</sub></td><td align="center" valign="middle" >C<sub>1</sub></td><td align="center" valign="middle" ></td></tr></tbody></table></table-wrap><p>with Sun Lei’s result [<xref ref-type="bibr" rid="scirp.83988-ref9">9</xref>] . Secondly, among all the three factors, ratio of solid to liquid was the most important factor which affected extraction yields because its value, the maximum range, was 1.07. The higher the ratio was, the larger the surface area of the solvent contact was. The influences of extraction time and solvent ratio were approximate, and were lower than that of solvent amount. However, they could not be neglected. At last, according to uniform design method, the best combination of experimental condition was A3B2C1, which meant the ratio of solid to liquid 1:2.5, extraction time 5 min, ratio of EA/BuOH 1:1, which was amazing the same to group 8<sup>th</sup>.</p></sec><sec id="s3_2"><title>3.2. The Contents of Phospholipids and Astaxanthin in Krill Oil Samples</title><p>Standard curves (<xref ref-type="fig" rid="fig2">Figure 2</xref>) were constructed for peak areas and concentrations of standards L-α-phosphatidylethanolamine (t<sub>R</sub> 3.9) and L-α-phosphatidylcholine (t<sub>R</sub> 6.7), respectively. A good linear correlation was observed in the concentration range of 0.2 - 1.8 mg/mL of L-α-phosphatidylcholine, and its equation of calibration curve was Y = 2462.7X − 95.488 (R<sup>2</sup> = 0.9987). While for L-α-phosphatidylethanolamine, linear correlation was observed between concentrations of 0.06 and 2.0 mg/mL, with the equation of calibration curve Y = 4554.5X − 30.893 (R<sup>2</sup> = 0.9989).</p><p>The phospholipid contents of the 9 samples obtained from the orthogonal experiment were detected by HPLC with standards of L-α-phosphatidylcholine</p><p>and L-α-phosphatidylethanolamine (<xref ref-type="table" rid="table3">Table 3</xref>), which can be separated from other impurities completely in orthogonal sample (<xref ref-type="fig" rid="fig1">Figure 1</xref>). The contents of L-α-phosphatidylcholine and L-α-phosphatidylethanolamine in the krill oils accounted for 25.79% - 38.79%, 0.92% - 3.54%, respectively. The results were close to the results of Bj&#248;rn Winther [<xref ref-type="bibr" rid="scirp.83988-ref10">10</xref>] . It should be mentioned that L-α-phosphatidylcholine was more than 90% of the total phospholipids.</p><p>The contents of astaxanthin in these samples were also determined by UV spectrophotometer. Standard curves were constructed for absorbance and concentrations of standard astaxanthin. A good linear correlation was observed in the concentration range of 0.12 - 12 &#181;g/mL. The equation of calibration curve was A = 0.1710C + 0.0601 (R<sup>2</sup> = 0.9956). The contents of astaxanthin in these krill oil samples accounted for 37.9 ~ 49.3 ppm. Astaxanthin was a kind of natural pigment in the E. superba, which was easier to be esterified. The average content is about 180 ppm (132 - 250 ppm) [<xref ref-type="bibr" rid="scirp.83988-ref11">11</xref>] . These experiment results were less thanthe average range. Therefore, to raise the contents of astaxanthin in extraction of E. superba will be the following research emphasis.</p><p>On the basis of all above, a feasible and effective extraction method of Antarctic krill oil with a solvent mixture of ethyl acetate and n-butanol were established, and modified by orthogonal test. It was found to extract krill oil with a high phospholipids content of 27.7% - 42.3%, together with a total oil yields of 4.15% - 6.18%.</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> The contents of astaxanthin and phospholipid of the krill oil samples</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >No.</th><th align="center" valign="middle" >Astaxanthin (ppm)</th><th align="center" valign="middle" >L-α-phosphatidylcholine (%)</th><th align="center" valign="middle" >L-α-phosphatidylethanolamine (%)</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >49.3</td><td align="center" valign="middle" >32.72</td><td align="center" valign="middle" >2.94</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >40.2</td><td align="center" valign="middle" >30.46</td><td align="center" valign="middle" >2.00</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >40.9</td><td align="center" valign="middle" >38.79</td><td align="center" valign="middle" >3.54</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >41.3</td><td align="center" valign="middle" >34.90</td><td align="center" valign="middle" >2.93</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >37.9</td><td align="center" valign="middle" >26.77</td><td align="center" valign="middle" >0.92</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >45.3</td><td align="center" valign="middle" >25.79</td><td align="center" valign="middle" >2.82</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >45.1</td><td align="center" valign="middle" >32.51</td><td align="center" valign="middle" >2.18</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >42.2</td><td align="center" valign="middle" >28.59</td><td align="center" valign="middle" >2.60</td></tr><tr><td align="center" valign="middle" >9</td><td align="center" valign="middle" >41.1</td><td align="center" valign="middle" >28.61</td><td align="center" valign="middle" >1.65</td></tr></tbody></table></table-wrap></sec></sec><sec id="s4"><title>Acknowledgements</title><p>Financial support of Central Public-interest Scientific Institution Basal Research Fund, CAFS (No. 2016HY-ZD0903) was greatly appreciated.</p></sec><sec id="s5"><title>Cite this paper</title><p>Tian, X.Q., Fan, C.Q., Liu, Z.D., Huang, H.I. and Lu, Y.N. (2018) An Effective Extract Method of Phospholipids from Antarctic Krill Euphausea superba. Open Journal of Marine Science, 8, 293-299. https://doi.org/10.4236/ojms.2018.82015</p></sec></body><back><ref-list><title>References</title><ref id="scirp.83988-ref1"><label>1</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Niu</surname><given-names> Z.A. </given-names></name>,<etal>et al</etal>. (<year>1999</year>)<article-title>Soybean Lecithin at Home and Abroad Market and Development</article-title><source> Cereals &amp; Oils</source><volume> 1</volume>,<fpage> 33</fpage>-<lpage>37</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.83988-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Zhao, X.-P., Wang, S., Hao, P.-F., Miao, J.-K., Liu, X.-F., Gao, H., Zhao, X.-Y. and Leng, K.-L. (2016) Optimization of Preparation of the Antarctic Krill Phospholipid Ginsenoside Phospholipid-Complex by Response Surface Methodology. Chinese Journal of Marine Drugs, 35, 72-80.</mixed-citation></ref><ref id="scirp.83988-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">An, H., Song, W.M. and Zhang, H.B. (2006) Phospholipid Chemistry and Application Technology. Chinese Metrology Press, Beijing.</mixed-citation></ref><ref id="scirp.83988-ref4"><label>4</label><mixed-citation publication-type="other" xlink:type="simple">Ali-Nehari, A. and Chun, B.S. (2011) Characterization of Purified Phospholipids from Krill (Euphausiasuperba) Residues Deoiled by Supercritical Carbon Dioxide. Korean Journal of Chemical Engineering, 29, 918-924. 
https://doi.org/10.1007/s11814-011-0273-4</mixed-citation></ref><ref id="scirp.83988-ref5"><label>5</label><mixed-citation publication-type="other" xlink:type="simple">Yan, Y.-Y., Zhang, K.-Y., Huang, J.-H., Liu, L.-F. and Wang, X.-G. (2012) Research Advance in Separation, Purification and Determination of Phospholipids. China Oils and Fats, 37, 61-65</mixed-citation></ref><ref id="scirp.83988-ref6"><label>6</label><mixed-citation publication-type="other" xlink:type="simple">Wang, H.-R., Kong, X.-Z. and Hua, Y.-F. (2012) Extraction and Analysis of Residual Lipids in Soybeanmeal. China Oils and Fats, 37, 84-87.</mixed-citation></ref><ref id="scirp.83988-ref7"><label>7</label><mixed-citation publication-type="other" xlink:type="simple">Zhang, J.-T., Lu, Y.-N., Yang, Q., Ma, L.-Y., Fan, C.-Q. and Tian, X.-Q. (2015) On the Extraction of Liposoluble Components from Aplidiumconstellatum. Marine Fisheries, 37, 264-269</mixed-citation></ref><ref id="scirp.83988-ref8"><label>8</label><mixed-citation publication-type="other" xlink:type="simple">Yang, C.-L., Shi, Y.-T. and Tang, Y.-Q. (2017) Orthogonal Test and Regression Analysis of the Strain on Silty Soil in Shanghai under Metro Loading. Environmental Earth Sciences, 75, 506</mixed-citation></ref><ref id="scirp.83988-ref9"><label>9</label><mixed-citation publication-type="other" xlink:type="simple">Sun, L., Zhou, D.-Q. and Sheng, X.-F. (2008) Nutrition and Safety Evaluation of Antarctic Krill. Marine Fisheries Research, 29, 57-64.</mixed-citation></ref><ref id="scirp.83988-ref10"><label>10</label><mixed-citation publication-type="other" xlink:type="simple">Bj?rn W., Nils, H. and Kjetil, B. (2011) Elucidation of Phosphatidylcholine Composition in Krill Oil Extracted from Euphausia superb. Lipids, 46, 25-36. 
https://doi.org/10.1007/s11745-010-3472-6 </mixed-citation></ref><ref id="scirp.83988-ref11"><label>11</label><mixed-citation publication-type="other" xlink:type="simple">Jing Z. (2012) Extraction and Purification of Antarctic Krill Phospholipids and Experimental Study of its Anti-Aging Effect (Qingdao). Ph.D. Thesis, Ocean University of China, Shanghai.</mixed-citation></ref></ref-list></back></article>