<?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">ABB</journal-id><journal-title-group><journal-title>Advances in Bioscience and Biotechnology</journal-title></journal-title-group><issn pub-type="epub">2156-8456</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/abb.2019.1010025</article-id><article-id pub-id-type="publisher-id">ABB-95887</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></subj-group></article-categories><title-group><article-title>
 
 
  New Ionic Liquids with Buffering and Chelating Abilities for Enzyme Engineering
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Guangnan</surname><given-names>Ou</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>Biyan</surname><given-names>He</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>College of Food and Biological Engineering, Jimei University, Xiamen, China</addr-line></aff><aff id="aff2"><addr-line>Fujian Provincial Key Laboratory of Food Microbiology and Enzyme Engineering, Xiamen, China</addr-line></aff><pub-date pub-type="epub"><day>14</day><month>10</month><year>2019</year></pub-date><volume>10</volume><issue>10</issue><fpage>320</fpage><lpage>330</lpage><history><date date-type="received"><day>16,</day>	<month>September</month>	<year>2019</year></date><date date-type="rev-recd"><day>20,</day>	<month>October</month>	<year>2019</year>	</date><date date-type="accepted"><day>23,</day>	<month>October</month>	<year>2019</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>
 
 
  Ionic liquids (ILs) with buffering and chelating abilities were designed and synthesized on the basis of ethylenediaminetetraacetic acid (EDTA) for the development of buffered enzymatic IL systems and for enzymatic reaction in heavy metal containing aqueous system. Transesterification activity of 
  Candida antarctica
   lipase B dissolved in the hydroxyl-functionalized IL was buffer dependent. High activity and outstanding stability was obtained with the buffered enzymatic IL systems for the transesterification. In heavy metal containing aqueous system, EDTA IL buffers as Hg
  <sup>2+</sup>
   chelators protected horseradish peroxidase (HRP) against Hg
  <sup>2+</sup>
  -induced denaturation and precipitation. Higher pH favored the protection, while at lower pH the protection diminished. We can conclude that the new ILs possess both buffering and chelating abilities.
 
</p></abstract><kwd-group><kwd>Ionic Liquid</kwd><kwd> EDTA</kwd><kwd> Buffer</kwd><kwd> Chelator</kwd><kwd> Lipase</kwd><kwd> Peroxidise</kwd><kwd> Heavy Metal</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Enzymes catalyze a wide variety of reactions best in heavy-metal-free aqueous environments and at physiological pH with exquisite selectivity and stereospecificity [<xref ref-type="bibr" rid="scirp.95887-ref1">1</xref>] . Thus, an appropriate buffer is needed to closely regulate the ionization state of ionizable groups of the enzyme in both aqueous and non-aqueous media. We have synthesized a new class of ionic liquids (ILs) with buffering behaviour that are referred to as IL buffers, which can be used for control of ionization state of enzymes in non-aqueous media [<xref ref-type="bibr" rid="scirp.95887-ref2">2</xref>] . Remarkable buffer dependence of the catalytic activities has been observed in hydrogenation of olefins [<xref ref-type="bibr" rid="scirp.95887-ref2">2</xref>] and selective hydrogenation of unsaturated aldehyde [<xref ref-type="bibr" rid="scirp.95887-ref3">3</xref>] in organic solvents and in ILs. Organic solvents are widely used with enzymes to improve the solubility of hydrophobic reactants and/or products and to shift reaction equilibria from hydrolysis toward synthesis [<xref ref-type="bibr" rid="scirp.95887-ref4">4</xref>] - [<xref ref-type="bibr" rid="scirp.95887-ref9">9</xref>] . With the emergence of ILs, the use of ILs as a new type of non-aqueous medium may offer a convenient solution to both the solvent emission and the catalyst recycling problem [<xref ref-type="bibr" rid="scirp.95887-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.95887-ref9">9</xref>] - [<xref ref-type="bibr" rid="scirp.95887-ref22">22</xref>] .</p><p>Increasing water contamination by heavy metals has prompted investigations to find ways to clean the environment and also to understand the mechanisms leading to metal toxicity, among which is enzyme inhibition. This inhibition was most often attributed to the reaction of the metal ions with the thiol groups of cysteine residues of the enzyme, resulting in the formation of mercaptides [<xref ref-type="bibr" rid="scirp.95887-ref23">23</xref>] [<xref ref-type="bibr" rid="scirp.95887-ref24">24</xref>] .</p><p>It was reported that peroxidases are inhibited by heavy metal ions at higher concentrations [<xref ref-type="bibr" rid="scirp.95887-ref25">25</xref>] and Hg<sup>2+</sup> ion is listed as the most effective inhibitor [<xref ref-type="bibr" rid="scirp.95887-ref26">26</xref>] [<xref ref-type="bibr" rid="scirp.95887-ref27">27</xref>] . Konyaeva et al. reported that Hg<sup>2+</sup> chelators like EDTA can protect hemoglobin against Hg<sup>2+</sup>-induced denaturation and precipitation [<xref ref-type="bibr" rid="scirp.95887-ref28">28</xref>] .</p><p>Like most biological buffers in use today, IL buffers were developed only for keeping the pH of a solution constant, which cannot protect enzymes against metal-induced denaturation and precipitation. We then designed and synthesized new ILs with both buffering and chelating abilities for enzymatic reactions in heavy metal containing aqueous system and in IL system.</p></sec><sec id="s2"><title>2. Materials and Methods</title><sec id="s2_1"><title>2.1. Materials</title><p>Candida antarctica lipase B (CALB, 10.9 U∙mg<sup>-</sup><sup>1</sup>), horseradish peroxidase (HRP, 150 U∙mg<sup>-</sup><sup>1</sup>), bis-tris-propane (BTP), guaiacol and ethyl butyrate were purchased from Sigma-Aldrich. Ethyl butyrate and n-butanol were analytical reagents and were dried by 3A molecular sieves before use. All other chemicals and reagents were of analytical grade. 1-buthyl-3-methyl-imidazolium chloride ([BMIM]Cl) and 1-(1-hydroxyethyl)-3-methyl-imidazolium tetrafluoroborate ([C<sub>2</sub>OHMIM] [BF<sub>4</sub>]) were synthesised according to published procedures [<xref ref-type="bibr" rid="scirp.95887-ref11">11</xref>] . [C<sub>2</sub>OHMIM] [BF<sub>4</sub>] was checked for the absence of chloride and acid. The IL was passed through a neutral alumina column, dried at 50˚C under reduced pressure for more than 18 h, and stored under dry N<sub>2</sub>.</p><p>The <sup>1</sup>H NMR and<sup> 13</sup>C NMR spectra were obtained on a Br&#252;ker AV-400 Fourier transform NMR spectrometer. <sup>1</sup>H NMR spectra were referenced to tetramethylsilane in CDCl<sub>3</sub>.</p></sec><sec id="s2_2"><title>2.2. pH Titration Procedure</title><p>Titration was carried out using a custom-built autotitrator. Place a magnetic stirring bar in the beaker and set the beaker over a magnetic stirrer. An appropriate amount of EDTA acid (1.0 mmol) was dissolved in 20 mL of water. Immerse the electrodes in the solution and start the stirring. 0.1 M [BMIM] [OH] solution was added by a peristaltic pump (Shanghai Hu Xi analysis instrument factory Co., Ltd., model HL-2) running at 1.0 mL∙min<sup>−1</sup>. The pH of the mixture was recorded with a pH meter (ORION, model 828) interfaced to a computer.</p></sec><sec id="s2_3"><title>2.3. Synthesis of EDTA IL Buffer</title><p>An aqueous solution of 1-buthyl-3-methyl-imidazolium hydroxide ([BMIM]OH) was prepared by passing [BMIM]Cl solution through a column filled with anion exchange resin, as described in the literature [<xref ref-type="bibr" rid="scirp.95887-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.95887-ref11">11</xref>] . The aqueous [BMIM]OH solution was then neutralized with EDTA acid in a beaker and the pH of the solution was adjusted to 3.90, 6.50, 8.50 or 9.80. The solution was evaporated at 50˚C under reduced pressure to give a viscous liquid, which was then vacuum dried at 50˚C for 18 h to afford EDTA IL buffer. NMR spectra of EDTA IL buffer: pH 9.80 <sup>1</sup>H NMR (400 MHz, D<sub>2</sub>O) δ: 7.368 (s, 4H, im-H), 7.320 (s, 4H, im-H), 4.088 (t, 8H, -CH<sub>2</sub>), 3.784 (s, 12H, im-CH<sub>3</sub>), 3.447 (s, 8H, N-CH<sub>2</sub>-COO-), 3.033 (s, 4H, N-CH<sub>2</sub>-CH<sub>2</sub>-N), 1.721 - 1.758 (m, 8H, -CH<sub>2</sub>), 1.199 - 1.217 (m, 8H, -CH<sub>2</sub>), 0.794 - 0.831 (t, 12H, -CH<sub>3</sub>); <sup>13</sup>C NMR (400MHz, D<sub>2</sub>O) δ: 175.703, 135.599, 123.385, 122.119, 57.238, 51.069, 49.200, 35.547, 31.212, 18.706, 12.600. pH 3.90 <sup>1</sup>H NMR (400 MHz, D<sub>2</sub>O) δ: 8.067 (s, 2H, im-H), 7.368 (s, 2H, im-H), 7.328 (s, 2H, im-H), 4.085 (t, 4H, -CH<sub>2</sub>), 3.796 (s, 6H, im-CH<sub>3</sub>), 3.782 (s, 8H, N-CH<sub>2</sub>-COO-), 3.580 (s, 4H, N-CH<sub>2</sub>-CH<sub>2</sub>-N), 1.717 - 1.754 (m, 4H, -CH<sub>2</sub>), 1.195 - 1.214 (m, 4H, -CH<sub>2</sub>), 0.790 - 0.827 (t, 6H, -CH<sub>3</sub>); <sup>13</sup>C NMR (400 MHz, D<sub>2</sub>O) δ: 170.500, 135.822, 123.4495, 122.169, 57.939, 51.569, 49.232, 35.602, 31.235, 18.721, 12.624.</p></sec><sec id="s2_4"><title>2.4. General Procedures of Enzymatic Transesterification in IL</title><p>CALB (1.2 mg) was dissolved in 500 μL of [C<sub>2</sub>OHMIM][BF<sub>4</sub>] (30 mg of EDTA IL buffer was added in the case of buffered medium) in a 5 mL flask. 110 μL (0.83 mmol) ethyl butyrate and 110 μL (1.21 mmol) n-butanol and 50 μL nonane (internal standard) were added. The reaction mixture was stirred at 40˚C in oil bath for 3 h. After the reaction was complete, the products was decanted from [C<sub>2</sub>OHMIM][BF<sub>4</sub>]. The organic phase was analyzed with a gas chromatograph equipped with an FID and a capillary column (SE-30, 30 m &#215; 0.32 mm &#215; 0.25 μm). The residual reactant mixture in IL phase was removed in vacuum at 40˚C for more than 1 h. The new cycle was restarted by addition of fresh substrate.</p></sec><sec id="s2_5"><title>2.5. HRP activity in Mercury Containing Aqueous System</title><p>HRP activity was measured by following the H<sub>2</sub>O<sub>2</sub>-dependent oxidation of guaiacol at 470 nm. Guaiacol stock solutions (1.0 mM) were prepared by dissolving guaiacol in 0.1 M buffer. For assays done in the presence of Hg<sup>2+</sup> ions, appropriate amounts of Hg(NO<sub>3</sub>)<sub>2</sub> stock solution were mixed with 0.1 M buffer and the pH was readjusted whenever required. H<sub>2</sub>O<sub>2</sub> stock solutions (300 mM) were prepared daily by appropriate dilution of 30% H<sub>2</sub>O<sub>2</sub> in distilled water. HRP solutions (10 μg/ml) were prepared by dissolving the enzyme in distilled water. The assay was performed by mixing 500 μL guaiacol stock solutions with 15 μL of HRP solution (final concentration 7.8 nM) and the mixture was then incubated at 298 K for 30 min. The reaction was started by adding 15 μL of 300 mM H<sub>2</sub>O<sub>2</sub>. The initial velocity (v<sub>0</sub>) of the oxidation of guaiacol was determined from linear plotting of the absorbance versus time, using an extinction coefficient of 2.66 &#215; 10 <sup>4</sup> M <sup>−1</sup>∙cm<sup>−1</sup> for guaiacol-derived oxidation product.</p><p>All assays were carried out at 298 K using a UV-Vis spectrophotometer (Unico, UV2800) which cell was connected to a thermostat.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Titration Profiles of EDTA</title><p>The titration profile of EDTA with [BMIM]OH in water expressed 3 buffering-like regions, which are centered at pH 3.90, 6.50 and 8.50, respectively (<xref ref-type="fig" rid="fig1">Figure 1</xref>).</p><p>Thus, we considered that it is possible to synthesize new ILs of buffering ability by neutralization of aqueous solutions of [BMIM]OH with aqueous solutions of EDTA at pH 3.90, 6.50 and 8.50, as illustrated in Scheme 1.</p></sec><sec id="s3_2"><title>3.2. Synthesis and Characterization of EDTA IL Buffer</title><p>The structure of EDTA IL buffers were shown in Scheme 1. The IL buffers were synthesized as previously reported [<xref ref-type="bibr" rid="scirp.95887-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.95887-ref11">11</xref>] and characterized by NMR. The characterization data of EDTA IL at pH 3.90 and pH 9.80 are consistent with the expected compositions and structures. The pH, the dilution value, and buffer values of EDTA IL buffers were summarized in <xref ref-type="table" rid="table1">Table 1</xref>. It can be seen that the ILs synthesized possess buffering ability and can be used for controlling the ionization of enzymes in both aqueous and non-aqueous media.</p><disp-formula id="scirp.95887-formula1"><graphic  xlink:href="//html.scirp.org/file/2-7301590x3.png"  xlink:type="simple"/></disp-formula><p>Scheme 1. Synthesis of EDTA IL buffer.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> pH, buffer values, and dilution values of the aqueous solution of EDTA IL buffers</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Buffer</th><th align="center" valign="middle" >pH</th><th align="center" valign="middle" >Concentration/mol∙L<sup>-</sup><sup>1</sup></th><th align="center" valign="middle" >Dilution value<sup>a</sup><sup>)</sup></th><th align="center" valign="middle" >Buffer value<sup>b</sup><sup>)</sup></th></tr></thead><tr><td align="center" valign="middle" >IL- 3.90</td><td align="center" valign="middle" >3.90</td><td align="center" valign="middle" >0.025</td><td align="center" valign="middle" >+0.01</td><td align="center" valign="middle" >0.004</td></tr><tr><td align="center" valign="middle" >IL- 6.50</td><td align="center" valign="middle" >6.50</td><td align="center" valign="middle" >0.025</td><td align="center" valign="middle" >+0.03</td><td align="center" valign="middle" >0.011</td></tr><tr><td align="center" valign="middle" >IL- 8.50</td><td align="center" valign="middle" >8.50</td><td align="center" valign="middle" >0.025</td><td align="center" valign="middle" >+0.03</td><td align="center" valign="middle" >0.002</td></tr></tbody></table></table-wrap><p>The structure of EDTA IL buffers, [ BMIM ] n + [ EDTA ] n − were shown in Scheme 1. The parameters were measured at room temperature. <sup>a</sup>Dilution value is defined as the change of pH on dilution with an equal volume of water. <sup>b</sup>The buffer value is defined as the number of moles of strong base required to change the pH of one liter of solution by one unit.</p></sec><sec id="s3_3"><title>3.3. Enzymatic Transesterification in the Presence of EDTA IL Buffer</title><p>Lipase-mediated transesterification is one of the economically viable clean technology for flavor ester production [<xref ref-type="bibr" rid="scirp.95887-ref29">29</xref>] . To test the activity of CALB lipase in dissolved form in ILs, we examined the CALB-catalyzed transesterification of ethyl butyrate with n-butanol. All the reactions were performed under the same conditions, 40˚C and 300 rpm, in this study to eliminate any temperature or mixing effects. The results showed that CALB afforded lower substrate conversion in pure [C<sub>2</sub>OHMIM][BF<sub>4</sub>] (8.7%). In contrast, CALB exhibited great transesterification activity in the buffered [C<sub>2</sub>OHMIM][BF<sub>4</sub>] (see <xref ref-type="fig" rid="fig2">Figure 2</xref>), indicating that the buffer was responsible for the rate enhancement.</p><p>The above results showed that the lipase activity is greatly affected by the IL and IL buffer. This is because the ionization constant of ionizable groups of the lipase is greatly affected by the solvent [<xref ref-type="bibr" rid="scirp.95887-ref30">30</xref>] . Thomazeau et al. reported that the acid HNTf<sub>2</sub> is more acidic in [BMIM][NTf<sub>2</sub>] and [BMIM][BF<sub>4</sub>] than in water</p><p>[<xref ref-type="bibr" rid="scirp.95887-ref31">31</xref>] . Thus, when CALB transfer from water to [C<sub>2</sub>OHMIM][BF<sub>4</sub>], the ionization state of the lipase will be changed, resulting in decrease of lipase activity. And addition of EDTA IL buffer can regulate the ionization state of ionizable groups of the lipase to the appropriate state. One can conclude that enzyme activity in ILs is also buffer dependent as in aqueous systems.</p><p>The recycling ability of the soluble CALB in buffered [C<sub>2</sub>OHMIM][BF<sub>4</sub>] under the above reaction conditions is illustrated in <xref ref-type="fig" rid="fig2">Figure 2</xref>. After each reaction, the reactant mixture in the upper layer and CALB-IL in the lower layer were separated by decantation. The CALB-IL phase was then evacuated to remove residual reactant mixture and charged for the next reaction without adding any new enzyme, IL, and buffer. The lipase activity dropped significantly during recycling in the presence of EDTA IL buffer of pH 3.90, suggesting that the lipase was gradually denatured in the acidic environment. However, the conversion of ethyl butyrate can maintain 75% of its initial value after 10 runs in the presence of EDTA IL buffer of pH 6.50 or pH 8.50, indicating that the dissolved CALB in the above buffered [C<sub>2</sub>OHMIM][BF<sub>4</sub>] is very stable.</p></sec><sec id="s3_4"><title>3.4. HRP Activity in Mercury Containing Aqueous System</title><p>Oxidative stress causes uncontrolled oxidation, resulting in the progressive deterioration and the collapse of organs and systems in the living organisms [<xref ref-type="bibr" rid="scirp.95887-ref32">32</xref>] . Peroxidases are important detoxifying enzymes serving to rid cells of excess</p><p>H<sub>2</sub>O<sub>2</sub>, Horseradish peroxidase (HRP) is one of the best characterized peroxidases [<xref ref-type="bibr" rid="scirp.95887-ref33">33</xref>] . The effects of Hg<sup>2+</sup> on HRP can be easily assayed through activity of H<sub>2</sub>O<sub>2</sub>-dependent oxidation, which can be assayed spectrophotometrically at 470 nm using the H<sub>2</sub>O<sub>2</sub>-dependent oxidation of guaiacol.</p><p><xref ref-type="fig" rid="fig3">Figure 3</xref> showed that EDTA IL buffers as Hg<sup>2+</sup> chelators protected HRP against Hg<sup>2+</sup>-induced denaturation and precipitation. Higher pH favored the protection, while at lower pH the protection diminished. Because the concentration of the deprotonated conjugate base of EDTA increases with the increase of pH of solution, its subsequent increased binding to Hg<sup>2+</sup> causes the protection of HRP against Hg<sup>2+</sup>-induced denaturation. On the contrary, there is almost no Hg<sup>2+</sup> chelators in BTP buffer system, thereby, Hg<sup>2+</sup> inhibition occurs. This chelating effect undoubtedly explained the difference in <xref ref-type="fig" rid="fig3">Figure 3</xref> and <xref ref-type="fig" rid="fig4">Figure 4</xref>.</p></sec></sec><sec id="s4"><title>4. Conclusion</title><p>In summary, ILs based on EDTA were synthesized by neutralization of [BMIM]OH with EDTA acid for the development of buffered enzymatic IL systems and for enzymatic reaction in heavy metal containing aqueous system. In buffered [C<sub>2</sub>OHMIM][BF<sub>4</sub>], transesterification activity of CALB is buffer dependent and CALB is stable during recycles. In EDTA IL buffer aqueous system, EDTA as Hg<sup>2+</sup> chelators protected HRP against Hg<sup>2+</sup>-induced denaturation and precipitation. Higher pH favored the protection, while at lower pH the protection diminished. We can conclude that the new ILs possess both buffering and chelating abilities and can be used for enzymatic applications.</p></sec><sec id="s5"><title>Data Availability</title><p>The data used to support the findings of this study are included within the article.</p></sec><sec id="s6"><title>Acknowledgements</title><p>We acknowledge the financial supports from the Natural Science Foundation of Fujian Province (2017J01635, 2019J01699), the Natural Science Foundation of China (41576085) and Fujian Provincial Key Laboratory of Food Microbiology and Enzyme Engineering (B18097-7).</p></sec><sec id="s7"><title>Conflicts of Interest</title><p>The authors declare that there is no conflict of interest regarding the publication of this paper.</p></sec><sec id="s8"><title>Cite this paper</title><p>Ou, G.N. and He, B.Y. (2019) New Ionic Liquids with Buffering and Chelating Abilities for Enzyme Engineering. 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