Subscriber access provided by UNIV OF NEBRASKA - LINCOLN
Article
Novel Nano/micro-Biocatalyst: Soybean Epoxide Hydrolase Immobilized on UiO-66-NH2 MOF for Efficient Biosynthesis of Enantipure (R)-1, 2-Octanediol in Deep Eutectic Solvents Shi-Lin Cao, Dong-Mei Yue, Xuehui Li, Thomas John Smith, Ning Li, Min-Hua Zong, Hong Wu, Yongzheng Ma, and Wen-Yong Lou ACS Sustainable Chem. Eng., Just Accepted Manuscript • DOI: 10.1021/ acssuschemeng.6b00777 • Publication Date (Web): 18 May 2016 Downloaded from http://pubs.acs.org on May 19, 2016
Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a free service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are accessible to all readers and citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.
ACS Sustainable Chemistry & Engineering is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.
Page 1 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Novel Nano/micro-Biocatalyst: Soybean Epoxide Hydrolase Immobilized on UiO-66-NH2 MOF for Efficient Biosynthesis of Enantipure (R)-1, 2-Octanediol in Deep Eutectic Solvents Shi-Lin Cao 1,2,3,4, Dong-Mei Yue 1,3, Xue-Hui Li 2, Thomas J Smith 5, Ning Li 3, Min-Hua Zong 2,3, Hong Wu 3, Yong-Zheng Ma 4,Wen-Yong Lou 1,3,*, 1
Lab of Applied Biocatalysis, School of Food Science and Engineering, South China
University of Technology, No. 13 Building, 381th Wushan Road, Guangzhou 510640, China. 2
School of Chemistry and Chemical Engineering, South China University of
Technology, No. 16 Building, 381th Wushan Road, Guangzhou 510640, China. 3
State Key Laboratory of Pulp and Paper Engineering, South China University of
Technology, Zaozhi Building, 381th Wushan Road, Guangzhou 510640, China. 4
Department of Applied Biology and Chemical Technology, The Hong Kong
Polytechnic University, Block Y, 1st Yuk Choi Rd, Kowloon, Hong Kong. 5
Biomolecular Sciences Research Centre, Sheffield Hallam University, Owen
Building, Howard Street, Sheffield, S1 1WB, UK *Corresponding author. Tel.: +86-20-22236669; fax: +86-20-22236669. E-mail address:
[email protected] (Prof. W. Y. Lou).
1 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 2 of 44
Abstract: The nano/micro-scale UiO-66-NH2 metal-organic framework (MOF) materials were successfully prepared with a uniform size of about 350-400 nm and structurally characterized.
Soybean epoxide hydrolase (SEH), a useful hydrolase for
synthesis of valuable vicinal diols, was for the first time efficiently immobilized onto the prepared UiO-66-NH2 MOF. The resulting novel nano/microbiocatalyst SEH@UiO-66-NH2 manifested high SEH loading (87.3 mg/g) and enzyme activity recovery (88.0%). The novel SEH@UiO-66-NH2 greatly surpassed the free SEH with resepct
to
pH-,
thermo
stabilities
and
tolerance
to
organic
solvents.
SEH@UiO-66-NH2 retained more than 17.6 U activity after 2 h incubation at 45oC, whereas free SEH maintained around 10.1 U activity under the same condition. After storage at 4 oC for 4 weeks, the prepared SEH@UiO-66-NH2 still retained around 97.5% of its initial activity. The significant enhancements resulted from the increase of structure rigidity of SEH@UiO-66-NH2, which was demonstrated by the secondary structure analysis of the enzyme. The optimun pH and tempearture of SEH@UiO-66-NH2 were significantly superior to the corresponding levels of its free counterpart.
Also,
SEH@UiO-66-NH2
manifested
markedly
enhanced
enzyme-substrate affinity and catalytic efficiency compared to free SEH, as supported by
a lower apparent Km value (6.5 vs. 19.2 mM) and a increased Vmax/ Km value
(8.0×10-3 vs.
5.8×10-3
min-1),
respectively.
Furthermore,
the
as-prepared
SEH@UiO-66-NH2, for the first time, was successfully applied as an efficient biocatalyst for the asymmetric hydrolysis of 1, 2-epoxyoctane to (R)-1,2-octanediol in novel deep eutectic solvent (DES) with a yield of around 41.4% and a product e.e. value of 81.2%. Remarkably, the nano/micro-scale UiO-66-NH2 MOFs as novel
ACS Paragon Plus Environment
Page 3 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
enzyme support materials are promising for enzyme immobilization and the prepared SEH@UiO-66-NH2 exhibited great potential for efficient biosynthesis of enantipure (R)-1,2-octanediol.
Keywords: Metal Organic Framework, Epoxide Hydrolase, Dipiptide, Deep eutectic solvent, Optically Active Vicinal Diols, Green Chemistry, Sustainable Chemistry.
INTRODUCTION Metal organic frameworks (MOFs), a class of hybrid material composed of metal ions and organic ligands (linkers) connected via coordinate bond to form two- or three-dimensional reticular crystalline structure1-3, have attracted increasing attention because of their unique diverse topologies, porosity and other favorable physical characteristics4. Presently, MOFs are mainly used in gas storage5-7, and homogeneous and
heterogeneous
catalysis8-10.
As
described
in
previous
reports11-13,
microperoxidase-11, laccase, trypsin and lipase have been successfully immobilized at Tb-meso MOF, MOF-199, MIL-88B and MIL-53(Al), respectively. The main immobilization methods used to date have been encapsulation14, and physical adsorption11, 15-17. When the enzymes was trapped into MOF mesopores, the reported immobilization process was time-consuming and in some cases 50 hours was necessary for the adsorption11. Also, the enzyme loading capacity of the MOF needed to be improved 16, 18. In view of the above limitations, chemical cross-linking has been used to attach enzyme covalently to the MOF, as well as complex post-synthesis
2 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
modification of MOF was utilized19. However, the post-synthesis modification only gave the carrier the limited active sites, which could influence the protein loading and relative activity recovery. As an alternative to the micro-scale MOFs described in the above reports, nano/micro-scale MOFs can be produced with uniform sizes and morphologies so that they can be well dispersed not only in aqueous media but also in other solvents20. Our recent study21 showed that the enzyme papain could be immobilized using formaldehyde onto a magnetic cellulose nano-material had enhanced activity, stability, catalytic efficiency and enzyme-substrate affinity22. This stimulated our interest to explore a relatively simple and chemically milder ways to prepare amino-functionalized MOFs with good solvent stability that could be used as the enzyme-carrier without further modification. Moreover, our previous literature indicated that both papain22 and pseudomonas cepacia lipase23 can be easily immobilized onto the surface of the nano-carrier via the precipitation-crosslinking method.
In order to explore the universality of this method, in the work described
here, we firstly immobilized enzyme onto the surface of the nano/micro-scale UiO-66-NH2 MOF via the precipitation-crosslinking method. The enzyme loading amount was improved and the immobilization time was shortened compared to previous studies. Epoxide hydrolase (EH) was chosen as the enzyme to test the as-prepared new nano/micro-material. Optically active vicinal diols and epoxides, which can be obtained from EH-mediated asymmetric hydrolysis of racemic epoxides, are important building blocks in the production of many bioactive compounds such as leukotriene, insect pheromones, steroides, β-blockers, adrenaline, nerve protectants, 3 ACS Paragon Plus Environment
Page 4 of 44
Page 5 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
and HIV protease inhibitors24, and the starting materials of ferroelectric liquid crystals25, as well as optically pure carboxylic acids, esters and other high-added-value
chemicals26.
Here,
hydrolysis
(R)-1,2-octanediol was used as the test reaction.
of
1,2-epoxyoctane
to
This product is used for treating
head louse infestations and as a starting material for production of ferroelectric liquid crystals. Compared with EHs from microorganisms, EHs from plants have many advantages such as a wide range of potential sources, low cost and facile preparation 27-31
. The observed product e.e. of epoxide hydrolysis catalyzed by EHs from
microorganisms is relatively low in some instances32-34. In contrast, it has been found that mung bean EHs can enantioselectively catalyze the hydrolysis of epoxides to produce enantiopure vicinal diols such as (R)-1-phenyl-1, 2-ethanediol, and (R)-p-nitrophenylglycol35-38. Nowadays, many researchers have focused on the enzymatic catalysis in deep eutectic solvent (DES)-containing systems. DESs are a kind of sustainable solvents, which are more biodegradable and less toxic than many traditional organic solvents, and can be conveniently obtained by mixing hydrogen bond donors and ammonium salt39. DESs have been efficiently used for several enzymatic processes such as lipase40, potato epoxide hydrolase41, protease22, and the result showed that the enzyme exhibited higher activity and stability in the presence of DESs. Widersten et.al
41
firstly reported the efficient use of DESs as co-solvents for
the hydrolysis of (1,2)-trans-2-methylstyrene oxide catalyzed by potato epoxide hydrolase with significantly increased solubility of substrate and regioselectivity of product. Therefore, it is of great interest to explore the catalytic performances of SEH in DES-containing co-solvent systems.
4 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 6 of 44
In the present study, we firstly carried out a comparative study on catalytic efficiency of EHs from five different plants for the asymmetric hydrolysis of 1, 2-epoxyoctane to (R)-1, 2-octanediol. Soybean epoxide hydrolase (SEH), a dimer and non-glycosylated protein with a molecular mass of about 31 kDa40, was found the most suitable enzyme for the reaction.
SEH was effectively immobilized onto the
surface of nano/micro-scale UiO-66-NH2 MOF support by using the precipitation and cross-linking method, and a comparative study was performed of the enzymatic hydrolysis of 1, 2-epoxyoctane catalyzed by the immobilized SEH (SEH@ UiO-66-NH2) and the free SEH. The obtained results show that SEH@ UiO-66-NH2 is an efficient biocatalyst for the asymmetric hydrolysis of 1,2-epoxyoctane to (R)-1,2-octanediol and that deep eutectic solvent (DES)-containing system can be used to further improve the product yield and the e.e. value. To the best of our knowledge, this is the first report of the asymmetric hydrolysis of 1, 2-epoxyoctane catalyzed by EHs from a plant source in DES-containing system.
EXPERIMENTAL SECTION Preparation of the UiO-66-NH2 metal-organic frameworks UiO-66-NH2 (all samples of UiO-66-NH2 were prepared by stirring unless stated otherwise): the synthesis of UiO-66-NH2 was performed by dissolving 1.4914g ZrCl4 (6.4mmol) and 1.1464g H2N-H2BDC in DMF (about 100 mL) in a beaker
42
. The
beaker was sealed with plastic wrap and placed in a preheated 80 oC oil-bath pan on a heating magnetic stirrer and stirred for 2h. The reaction was then heated to 100 oC for 4h. The reaction was cooled in air to room temperature and filtered. After washing 5 ACS Paragon Plus Environment
Page 7 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
three times with ethanol, the product was dried at 70 oC overnight in a drying oven. The resulting pale yellow powder was the metal-organic frameworks UiO-66-NH2. Preparation of the immobilized SEH (SEH@UiO-66-NH2) SEH immobilized onto UiO-66-NH2 (SEH@UiO-66-NH2) was prepared as follows. The as-prepared UiO-66-NH2 MOF (50 mg) was mixed with crude SEH preparation (5 mg of crude protein containing 0.625 mg of SEH) in PBS (phosphate buffer saline, 2ml, 50 mmol/L, pH 7.5), followed by adding 100% saturated ammonium sulfate solution (to give 80% final saturation) to precipitate the enzyme under magnetic stirring for 30 min at 4 oC. Then an appropriate amount of 25% glutaraldehyde (GA) was injected into the above mixture and stirred to cross-link the enzyme to the UiO-66-NH2 MOF. After cross-linking, the SEH@UiO-66-NH2 was then washed at least 3 times with PBS (50 mmol/L, pH 7.5) containing 10% glucose (m/v) and stored at 4 oC for subsequent use. The conditions to immobilize the enzyme onto the UiO-66-NH2 support, including GA concentration, cross-linking time and mass ratio of SEH to UiO-66-NH2 were studied. Assay of SEH activity The initial activity of the free SEH and the SEH@UiO-66-NH2 was determined as follows: a given amount of crude SEH protein or immobilized SEH was dispersed in 4 mL PBS buffer (50mmol/L, pH 6.75) containing 1,2-epoxyoctane (10mmol/L). The reaction was conducted for 10 min at 200r/min and 37.5 oC. Then, a sample (50µL) was taken out and the product was extracted from the sample with equivalent
6 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ethyl acetate. The product concentration was analyzed by GC described below. One unit (U) of enzyme activity (initial reaction rate) was defined as the amount of enzyme required to catalyze the release of 1 µM 1, 2-octanediol per min under the given conditions. For the immobilized SEH, the relative activity recovery was calculated as below:
Relative activity recovery % =
ℎ ℎ ! ℎ ℎ "
Enzymatic properties of free SEH and SEH@UiO-66-NH2 Optimal pH and temperature: the activities were measured according to the method described above over a pH range from 6.0 to 8.5 and a temperature range from 25 to 50 oC. Thermo-stability: 10.0 mg of crude SEH protein containing 1.25 mg of SEH or 125 mg of SEH@UiO-66-NH2 (containing 10 mg of crude SEH protein) were incubated in PBS (50 mmol/L, pH 6.7) at a range of temperatures (20–45oC) for 2 h, and the residual activity was determined as above. pH-stability: 10.0 mg of crude SEH protein containing 1.25 mg of SEH or 125 mg of SEH@UiO-66-NH2 (containing 10 mg of crude SEH protein) with various pH values (6.0 – 8.0) for 2 h at 37 oC, and the residual activity was determined as above. Tolerance to organic solvent: 10.0 mg of crude SEH protein containing 1.25 mg of SEH or 125 mg of SEH@UiO-66-NH2 (containing 10 mg of crude SEH protein) were incubated in 4 mL of various hydrophobic organic solvents (ethyl acetate, 7 ACS Paragon Plus Environment
Page 8 of 44
Page 9 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
n-octyl alcohol, isopropyl ether, cyclohexane, n-hexane) at 37.5 oC for 2 h, and the residual activity of the enzyme was assayed as above. The initial activity was defined as 100%. Storage-stability: the immobilized enzyme SEH@UiO-66-NH2 was stored at 4 oC for a range time periods, and then the residual activity of the enzyme was assayed as above. The activity of newly prepared immobilized was defined as 100%. Apparent kinetics parameters: the kinetic parameters of free SEH and SEH@UiO-66-NH2 were determined according to the previous study36 with varied concentrations of 1,2-epoxyoctane from 1 to 25 mmol/L in PBS (50 mmol/L, pH 6.7) at 37.5 oC. 8 mg of SEH was used to start the reaction in each case. The maximum reaction rate (Vmax) and the Michaelis-Menten constant (Km) were calculated from Hanes-Woolf plots. Biocatalytic asymmetric hydrolysis of 1,2-epoxyoctane with SEH@UiO-66-NH2 in aqueous and DES-containing systems Aqueous buffer system: 4 mL of PBS (50 mmol/L, pH 6.7) containing 2% (v/v) DMSO and 5 mmol/L 1, 2-epoxyoctane was added into a 25-mL Erlenmeyer flask capped with a septum. After the mixture was incubated in a water-bath shaker for 5 min at 37.5 oC, the reaction was initiated by adding 15.0 mg of crude SEH protein containing 1.875 mg of SEH or 187.5 mg of SEH@UiO-66-NH2 (containing 15.0 mg of crude SEH protein) to the system. Samples (60µL) were taken at specified time intervals. The product was extracted with an equal volume of ethyl acetate
8 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
containing 4’-chloroacetophenone as the internal standard and subsequently was analyzed by GC-2010. DESs containing system: 4 mL of the system consisting of PBS (50mmol/L, pH 7.0), and the four DESs above (15%, v/v) was contained in a 25-mLErlenmeyer flask capped with a septum. The reaction was started by adding 187.5 mg of SEH@UiO-66-NH2 (containing 15 mg of crude SEH protein) into the flask after incubated for 5 min at 40 oC. The samples were handled as those taken from the aqueous buffer system.
RESULTS AND DISSCUSSION Characterization of UiO-66-NH2 MOFs The UiO-66-NH2 MOFs were prepared and the resulting powders were yellow (Figure 1A). The morphologies of the MOFs were characterized via scanning electron microscopy (SEM) (Figure 1B). The size of the UiO-66-NH2 was shown via SEM to be uniform at about 350-400 nm. Then the materials were characterized by FTIR and XRD. The FTIR spectrum (Figure 2) was recorded to confirm the chemical composition of the nano/micro-composites. The peaks at 3375 and 3460 cm-1 were identified as the asymmetric and symmetric N-H stretching of the MOF (Figure 2). The vibration frequency at approximately 1656 cm-1 was assigned to the N-H bending vibration. The observed bending signals at 1388 cm-1 are typical frequencies of strong C-N stretching absorption peaks of aromatic amines (Figure 2). The assignments of 9 ACS Paragon Plus Environment
Page 10 of 44
Page 11 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
these spectroscopic features were further confirmed by FTIR spectrum of the model compound NH2-H2BDC and the results agreed well with the above bands42-43. The Raman spectrum of UiO-66-NH2 (Figure S1) illustrated the fluorescence of the as-prepared MOF, which was also consistent with a previous report in the literature 42. The XRD pattern of nano/micro-scale UiO-66-NH2 (Figure 5A1) was in accordance with a previous report42 and our simulated XRD pattern (FigureS2). These results indicated the phase purity of our as-synthesized UiO-66-NH2 support. Preparation and Characterization of SEH@ UiO-66-NH2 Five EHs from different plant sources were investigated as biocatalysts for the asymmetric hydrolysis of 1, 2-epoxyoctane. As shown in Table S1, in spite of relatively lower activity towards 1, 2-epoxyoctane than EHs from mung bean, jumbie bean or cow gram (23.6 U vs. 29.5-47.3 U), EH from soybean (SEH) exhibited the highest enantioselectivity and afforded the highest e.e. value of the product (R)-1, 2-octanediol (84.9% vs. 30.6-76.1%) among all the examined EHs. Therefore, SEH was selected for further study. Additionally, the electrophoresis analysis showed that the content of pure SEH in crude SEH protein and the molecular mass of SEH were about 12.5% and 31 kDa, respectively, which was similar with the previous report44. The immobilization of SEH onto UiO-66-NH2 is illustratedin Scheme 1. Glutaraldehyde (GA) was used as cross-linker because it is known from previous studies that GA can easily access reactive groups within the protein and cross-link them to amino groups as found on the support45. As can be seen in Figure S3, the optimal cross-linker concentration was approximately 130 10 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
mmol/L, with a relative activity recovery of 82.9%. The optimal cross-linking time was about 120 min (Figure S4). As indicated by Figure S5, the mass ratio of UiO-66-NH2 to SEH which was optimal for SEH immobilization was 10:1 (with relative activity recovery being 88.0% and the amount of crude SEH protein loaded onto the MOF being about 87.3 mg crude SEH protein /g UiO-66-NH2). Also, the SEM analysis showed that the SEH@UiO-66-NH2 had a relatively regular spherical shape of about 500 nm with smooth surface (Figure 3). The size of the immobilized SEH (SEH@UiO-66-NH2) relative to the support UiO-66-NH2 was increased from about 400 nm to 500 nm, due to the loading of SEH onto the surface of the MOF support. The average size of the SEH@UiO-66-NH2, measured by dynamic light scattering (DLS) at 25 oC, was around 465.2 nm (Figure S6A). The prepared SEH@UiO-66-NH2 well dispersed in the solution of DES and no significantly amorphous aggregates was observed (Figure S6B). FTIR, XRD were also used to characterize the SEH@ UiO-66-NH2. The N-H bending vibration peak at 1656 cm-1 of UiO-66-NH2 (Figure 2) shifted to 1652 cm-1 (Figure 4) after immobilization, indicating that SEH had bonded onto the surface of MOFs by cross-linking. The carrier of the immobilized enzymes (Figure 5B1) retained the crystal integrity of MOFs based on XRD (Figure 5A1 and Figure S2). It is well known that the degradation of many MOFs generally occurs in the presence of water as well as the hydrophilic solvents, possibly resulting from the relatively weak coordination bond strength of MOFs46. Recently, deep eutectic 11 ACS Paragon Plus Environment
Page 12 of 44
Page 13 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
solvents (DESs), relatively hydrophilic solvents, have gained much attraction as green media for biocatalytic processes22. Moreover, the SEH@UiO-66-NH2-catalyzed asymmetric hydrolysis of 1, 2-epoxyoctane will be conducted in DES-containing reaction systems in subsequent investigation. Therefore, it is necessary to study the stability of the support MOF and the immobilized enzyme (SEH@UiO-66-NH2 MOF) in various DESs. To examine the structural stability of the MOF, the XRD analysis for the support materials was performed after being exposed to the reaction media (PBS and DESs) for 2 h at 40 oC (Figure 5). The XRD diffraction peaks depicted in Figure 5A2 and 5B2 were slightly broaden, mainly because of the coordination ability of phosphate to the Zr-clusters47. However, the prepared UiO-66-NH2 MOF still maintained the structural stability, possibly due to the low amount of phosphate (50 mM) in the
solvent system47. No significant change of XRD spectra was observed
after being treated by four kinds of DES(ChCl (Choline Chloride) :Uera; ChCl : Glycerol; ChCl : Xylitol; ChCl : Ethylene glycol; Figure 5A2- Figure 5A6 and Figure 5B2- Figure 5B6). These results showed that both UiO-66-NH2 and SEH@ UiO-66-NH2 displayed structural stability in the four kinds of DES examined. Catalytic Performance of SEH@UiO-66-NH2 The effects of pH on the activity of free and immobilized enzymes were depicted in Figure 6, the optimal pH value for free SEH was 6.5 (18.9 U/mg SEH), while that of SEH@UiO-66-NH2 was 7.0 (16.6 U/mg SEH). The reason for this may be that22 the cross-linking between GA and the basic residues of enzyme changed the ionization state of protein functional groups in the microenvironment around the catalytic site of
12 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 14 of 44
the enzyme or the surface –NH2 groups of enzyme carriers, resulting in the alkaline shift of the optimal pH value of the immobilized enzyme46. Besides a higher relative activity (72.3% vs 52.4%), the as-prepared SEH@ UiO-66-NH2 exhibited a higher absolute activity of enzyme than free SEH (12.0 U/mg SEH vs 9.9 U/mg SEH) in PBS (50 mM, pH 8.0), which was consistent with the observation that the immobilization usually stabilizes enzymes against deactivation 48. The effects of assay temperature on the activity of free and immobilized enzymes were shown in Figure 7. The optimum temperature for the hydrolysis activity was 35oC for free SEH (17.6 U/mg SEH) and shifted to 40 oC for SEH@UiO-66-NH2 (16.6 U/mg SEH). Also, the SEH@UiO-66-NH2 retained more than 83.2% of relative activity (13.8 U/mg SEH) at 50 oC, while the free SEH maintained only about 58.1% of relative activity (11.0 U/mg SEH). The change in optimal temperature may have been due to a decline in the enzyme conformational flexibility and an improvement in SEH heat resistance after covalent cross-linking of the enzyme by GA during the immobilization process49-50. The kinetic behaviour of free SEH and SEH@ UiO-66-NH2 were compared (Table S2). It was found that the SEH-catalyzed hydrolysis of 1, 2-epoxyoctane followed the Michaelis-Menten model. The apparent Vmax of the SEH@ UiO-66-NH2 was lower than that of free SEH (5.2 × 10-2
vs. 11.2
×10-2 mM min-1) and the apparent kinetic parameter Km of SEH@ UiO-66-NH2 was also lower than that of free SEH (6.5 vs. 19.2 mM), demonstrating an
13 ACS Paragon Plus Environment
Page 15 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
increase in apparent enzyme-substrate affinity of the immobilized SEH49. One possible explanation for this observation would be a change of the three-dimensional structure of SEH upon immobilization making it easier for the substrate to access the enzyme’s active site. In addition, the catalytic efficiency Vmax/ Km value of SEH@ UiO-66-NH2 was higher than that of free enzyme (8.0 × 10-3 vs 5.8 × 10-3 min-1). It was of interest to investigate the internal mass transfer of SEH@UiO-66-NH2. The effectiveness factor #$ of SEH@UiO-66-NH2 was calculated to be about 0.954. The Thiele modulus (%) was determined to be around
0.285.
The
results
showed
that
the
rate
of
the
SEH@UiO-66-NH2-catalyzed reaction was limited by internal mass transfer to a moderate extent. SEH@ UiO-66-NH2 exhibited a higher pH-stability over a wider pH range (from 6.0 to 8.0) than free SEH Figure 8, most likely due to stabilization of the enzyme by cross-linking. When the SEH@UiO-66-NH2 was incubated at pH 7 for 2 h, it retained more than 95.1% of the relative activity (15.4 U/mg SEH) of its activity, whereas less than 82.9% of relative activity (14.1 U/mg SEH) remained with free enzyme under the same conditions. As can be seen in Figure 9, SEH@UiO-66-NH2 exhibited higher thermal stability than its free counterpart in the temperature range investigated. When the SEH@UiO-66-NH2 was incubated at 45oC for 2 h, it retained more than 84.6% of the relative activity (14.1 U/mg SEH) of its activity, whereas less than 42.8% of relative activity (8.1 U/mg SEH) remained with free enzyme under the
14 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
same conditions. Among the five hydrophobic organic solvents (Figure S7) examined, n-hexane showed the least toxicity to both free and immobilized enzyme. The residual activity of SEH@ UiO-66-NH2 was 7.7% higher than that of the free SEH in n-hexane. Previous research in our group showed that organic solvents with higher polarity can more significantly damage the native structure of the enzyme and result in rapid deactivation of the enzyme51.In general, SEH@MOF showed somewhat better solvent tolerance to all these five solvents compared with its free counterpart. This higher organic solvent tolerance after immobilization may have been mainly due to the increased structural rigidity of the enzyme after being immobilized onto the UiO-66-NH2 support. Finally, after storing at 4 oC for 4 weeks, the immobilized enzyme still had 97.5% relative activity (20.3U) (Table S3). FTIR spectroscopy is a useful tool for the study of the secondary structure (conformation)- catalytic performance relationships of enzyme52-53. From the amide I band (1600-1700 cm-1) in FTIR spectrum, it is possible to estimate the secondary structure content of the free and immobilized enzymes. From Figure 10, it is apparent that the secondary structure of the enzyme changed significantly after immobilization. The comparison of the secondary structure content of SEH and SEH@UiO-66-NH2 shows that the amount of α-helixes sharply increased (34.4% vs 19.4%) upon immobilization, and this is consistent with the increase in the rigidity of the enzymes’ structure that was inferred from the observed increased stability of the immobilized enzyme.The α-helix content of the protein may reflect the structural rigidity of
15 ACS Paragon Plus Environment
Page 16 of 44
Page 17 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
enzyme, which may play an important role in the stability of the enzyme to pH, temperature and organic solvents54-56. In the present study, FTIR results indicated that the enhancement in the stability of SEH@UiO-66-NH2 could be largely attributed to the increase in the structural rigidity of the enzyme after immobilization. Biocatalytic asymmetric hydrolysis of 1,2-epoxyoctane with SEH@UiO-66-NH2 in aqueous and DES-containing systems. As showed in Scheme 2, SEH preferentially catalyzed the hydrolysis of the (R)-1,2-epoxyoctane to produce (R)-1, 2-octanediol. When the concentration of (R)-isomer is low, the SEH could also hydrolyse the (S)-isomer to produce the opposite configuration of the product. Hence the e.e. of the product decreased with decreasing concentration of (R)-1,2-epoxyoctane substrate. As a result, we chose conditions of high substrate concentration that gave a relatively high yield and e.e. as the optimal reaction. Figure 11A displays the time course of (R)-1, 2-octanediol with free and immobilized SEH in phosphate buffer. Compared with the yield and product e.e. of free SEH (yield 41.5%, e.e. 78.7), the immobilized SEH has higher enantioselectivity (yield 41.4%, e.e. 81.2%). This may be due to the structural changes of SEH during the immobilization process 57. Then we studied this hydrolysis reaction in four DES-containing systems. It is apparent from Figure 11 that ChCl: Urea was the optimal DESs for asymmetric hydrolysis of 1, 2-epoxyoctane. Compared with phosphate buffer solution, ChCl: Uera system gave similar yield (41.2% vs 41.4%) but somewhat higher product e.e. (84.7% vs 81.2%), which was in accordance with our previous experience of whole-cell 16 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 18 of 44
catalysed reduction reactions in similar solvent systems. Although as a hydrogen bond donor the alkaline urea solution may deactivate the enzymes, this effect may be mitigated since the ChCl and urea in the DES are expected to bind to one another via a hydrogen-bonded network58. Furthermore, in the DES (ChCl: Urea) the product e.e. value increased and this solvent system may have additional advantages such as increasing the solubility of the substrate.
Conclusion In summary, the main achievements of this work are as follows: (1) epoxide hydrolase was for the first time immobilized onto the surface of the nano/microscale amino-functionalized MOFs rather than internal to the MOFs; (2) immobilized soybean epoxide hydrolase (SEH) was prepared for the first time and its enzymatic properties were studied; (3) SEH@ UiO-66-NH2 was prepared and used as an efficient
biocatalyst
for
asymmetric
hydrolysis
of
1,2-epoxyoctane
to
(R)-1,2-octanediol in DESs-containing system to further improve the yield and the product e.e.; (4) the stability of UiO-66-NH2 MOF in four DESs was investigated and the immobilised biocatalyst was found to have high catalytic efficiency and stability in the asymmetric hydrolysis of 1, 2-epoxyoctane to (R)-1, 2-octanediol in DES-containing media with high product yield and product e.e. value (yield 41.4%, e.e. 81.2%).
Supporting Information The method and materials: preparation of epoxy hydrolases (EHs) crude protein; 17 ACS Paragon Plus Environment
Page 19 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
screening of EHs from different plant sources for enzymatic asymmetric hydrolysis of 1,2-epoxyoctane; analytic methods; The structural stability of MOFs and SEH@UiO-66-NH2 in aqueous buffer and DES-containing systems; determination of internal mass transfer parameters; preparation of the immobilized SEH for in absence of UiO-66-NH2; Supplementary Table: Results of the asymmetric hydrolysis of 1,2-epoxyoctane catalyzed by epoxide hydrolases from different sources (Table S1). Apparent kinetic parameters of free enzyme and immobilized enzyme (Table S2). The storage stability of the immobilized enzyme (Table S3). Supplementary Figure: Raman spectrum of UiO-66-NH2 (Figure S1). XRD of the simulated UiO-66-NH2 (Figure S2). The effect of glutaraldehyde concentration on relative activity recovery (Figure S3). The effect of cross-linking time on relative activity recovery (Figure S4). The effect of MOF and SEH mass ratio on relative activity recovery (Figure S5). The DLS analysis of SEH@UiO-66-NH2 (Figure S6A). SEH@UiO-66-NH2 dispersed in ChCl: Urea DES solution (Figure S6B). Organic solvent tolerance of free and immobilized enzymes (Figure S7).This information is available free of charge via the Internet at http: //pubs.acs.org.
ASSOCIATED CONTENT Corresponding Author *Prof. W.-Y. Lou. Tel.: +86-20-22236669. Fax: +86-20-22236669. E-mail:
[email protected].
18 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Author Contributions The manuscript was written through contributions of all authors. All authors have given approval to the final version of the manuscript. Funding Sources The Program of State Key Laboratory of Pulp and Paper Engineering (2015C04), the National Natural Science Foundation of China (21336002; 21222606; 21376096), the Key Program of Guangdong Natural Science Foundation (S2013020013049), the Fundamental Research Funds for the Chinese Universities (2015PT002; 2015ZP009), and the Open Funding Project of the State Key Laboratory of Bioreactor Engineering, SCUT Doctoral Student Short-Term Overseas Visiting Study Funding Project. Note The authors declare no competing financial interest.
ACKNOWLEDGEMENT We wish to thank the Program of State Key Laboratory of Pulp and Paper Engineering (2015C04), the National Natural Science Foundation of China (21336002; 21222606; 21376096), the Key Program of Guangdong Natural Science Foundation (S2013020013049), the Fundamental Research Funds for the Chinese Universities (2015PT002; 2015ZP009), and the Open Funding Project of the State Key Laboratory of Bioreactor Engineering for partially funding this work. We also thank SCUT
19 ACS Paragon Plus Environment
Page 20 of 44
Page 21 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Doctoral Student Short-Term Overseas Visiting Study Funding Project.
20 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
REFERENCE
(1) Zhou H.-C., Long J.R., Yaghi O.M. Introduction to Metal-Organic Frameworks. Chem. Rev., 2012, 112: 673-674 (2) Yaghi O.M., O'Keeffe M., Ockwig N.W., Chae H.K., Eddaoudi M., Kim J. Reticular Synthesis and the Design of New Materials. Nature, 2003, 423: 705-714 (3) Imaz I., Rubio-Martínez M., An J., Sole-Font I., Rosi N.L., Maspoch D. Metal–Biomolecule Frameworks (Mbiofs). Chem. Commun., 2011, 47: 7287-7302 (4) Stock N., Biswas S. Synthesis of Metal-Organic Frameworks (Mofs): Routes to Various Mof Topologies, Morphologies, and Composites. Chem. Rev., 2011, 112: 933-969 (5) Czaja A.U., Trukhan N., Müller U. Industrial Applications of Metal–Organic Frameworks. Chem. Soc. Rev., 2009, 38: 1284-1293 (6) Greathouse J.A., Kinnibrugh T.L., Allendorf M.D. Adsorption and Separation of Noble Gases by Irmof-1: Grand Canonical Monte Carlo Simulations. Ind. Eng. Chem. Res., 2009, 48: 3425-3431 (7) Kanoo P., Gurunatha K.L., Maji T.K. Versatile Functionalities in Mofs Assembled from the Same Building Units: Interplay of Structural Flexibility, Rigidity and Regularity. J. Mater. Chem., 2010, 20: 1322-1331 (8)Savonnet M., Aguado S., Ravon U., Bazer-Bachi D., Lecocq V., Bats N., Pinel C., Farrusseng D. Solvent Free Base Catalysis and Transesterification over Basic Functionalised Metal-Organic Frameworks. Green Chem., 2009, 11: 1729-1732 (9) Sun C.-Y., Liu S.-X., Liang D.-D., Shao K.-Z., Ren Y.-H., Su Z.-M. Highly Stable Crystalline Catalysts Based on a Microporous Metal− Organic Framework and
21 ACS Paragon Plus Environment
Page 22 of 44
Page 23 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Polyoxometalates. J. Am. Chem. Soc., 2009, 131: 1883-1888 (10)
Chen J., Li K., Chen L., Liu R., Huang X., Ye D. Conversion of Fructose into
5-Hydroxymethylfurfural Catalyzed by Recyclable Sulfonic Acid-Functionalized Metal–Organic Frameworks. Green Chem., 2014, 16: 2490-2499 (11)
Lykourinou V., Chen Y., Wang X.-S., Meng L., Hoang T., Ming L.-J.,
Musselman R.L., Ma S. Immobilization of Mp-11 into a Mesoporous Metal–Organic Framework, Mp-11@ Mesomof: A New Platform for Enzymatic Catalysis. J. Am. Chem. Soc., 2011, 133: 10382-10385 (12)
Xie B., Jia H., Xie Y., Wei P. Immobilized Laccase and Its Properties by
Metal Organic Framework Mof-199. Chinese J. Bioproc. Eng., 2011, 5: 003.. (13)
Liu W.L., Yang N.S., Chen Y.T., Lirio S., Wu C.Y., Lin C.H., Huang H.Y.
Lipase ‐ Supported Metal – Organic Framework Bioreactor Catalyzes Warfarin Synthesis. Chem. Eur. J., 2015, 21: 115-119 (14)
Larsen R.W., Wojtas L., Perman J., Musselman R.L., Zaworotko M.J.,
Vetromile C.M. Mimicking Heme Enzymes in the Solid State: Metal–Organic Materials with Selectively Encapsulated Heme. J. Am. Chem. Soc., 2011, 133: 10356-10359 (15)
Chen Y., Lykourinou V., Hoang T., Ming L.-J., Ma S. Size-Selective
Biocatalysis of Myoglobin Immobilized into a Mesoporous Metal–Organic Framework with Hierarchical Pore Sizes. Inorg. Chem., 2012, 51: 9156-9158 (16)
Liu W.-L., Lo S.-H., Singco B., Yang C.-C., Huang H.-Y., Lin C.-H. Novel
Trypsin–Fitc@ Mof Bioreactor Efficiently Catalyzes Protein Digestion. J. Mater. Chem. B, 2013, 1: 928-932 22 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
(17)
Chen Y., Lykourinou V., Vetromile C., Hoang T., Ming L.-J., Larsen R.W.,
Ma S. How Can Proteins Enter the Interior of a Mof? Investigation of Cytochrome C Translocation into a Mof Consisting of Mesoporous Cages with Microporous Windows. J. Am. Chem. Soc., 2012, 134: 13188-13191 (18)
Huo J., Aguilera-Sigalat J., El-Hankari S., Bradshaw D. Magnetic Mof
Microreactors for Recyclable Size-Selective Biocatalysis. Chem. Sci., 2015, (19)
Shih Y.H., Lo S.H., Yang N.S., Singco B., Cheng Y.J., Wu C.Y., Chang I.,
Huang H.Y., Lin C.H. Trypsin‐Immobilized Metal–Organic Framework as a Biocatalyst in Proteomics Analysis. ChemPlusChem, 2012, 77: 982-986 (20)
Luan Y., Qi Y., Gao H., Zheng N., Wang G. Synthesis of an
Amino-Functionalized Metal-Organic Framework at a Nanoscale Level for Gold Nanoparticle Deposition and Catalysis. J. Mater. Chem. A, 2014, 2: 20588-20596 (21)
Cao S.-L., Li X.-H., Lou W.-Y., Zong M.-H. Preparation of a Novel
Magnetic Cellulose Nanocrystal and Its Efficient Use for Enzyme Immobilization. J. Mater. Chem. B, 2014, 2: 5522-5530 (22)
Cao S.-L., Xu H., Li X.-H., Lou W.-Y., Zong M.-H. Papain@Magnetic
Nanocrystalline Cellulose Nanobiocatalyst: A Highly Efficient Biocatalyst for Dipeptide Biosynthesis in Deep Eutectic Solvents. ACS Sus. Chem. Eng., 2015, 3: 1589-1599 (23)
Cao S.-L., Huang Y.-M., Li X.-H., Xu P., Wu H., Li N., Lou W.-Y., Zong
M.-H. Preparation and Characterization of Immobilized Lipase from Pseudomonas Cepacia onto Magnetic Cellulose Nanocrystals. Sci. Rep., 2016, 6: (24)
Mateo L.F.S.a.C. Improvement of the Epoxidehydrolase Properties for the 23 ACS Paragon Plus Environment
Page 24 of 44
Page 25 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Enantioselective Hydrolysis of Epoxides. Cur. Org. Chem., 2013, 17: 744-755 (25)
Crosby J. Chirality in Industry—an Overview. Chiral. Ind., 1992, 1-66
(26)
Chen Y., Chen C., Wu X. Dicarbonyl Reduction by Single Enzyme for the
Preparation of Chiral Diols. Chem. Soc. Rev., 2012, 41: 1742-1753 (27)
Kumar R., Wani S.I., Chauhan N.S., Sharma R., Sareen D. Cloning and
Characterization of an Epoxide Hydrolase from Cupriavidus Metallidurans-Ch34. Protein Expres. Purif., 2011, 79: 49-59 (28)
Martins M.P., Mouad A.M., Boschini L., Seleghim M.H.R., Sette L.D., Porto
A.L.M. Marine Fungi Aspergillus Sydowii and Trichoderma Sp. Catalyze the Hydrolysis of Benzyl Glycidyl Ether. Mar. Biotechnol., 2011, 13: 314-320 (29)
Woo J.-H., Lee E.Y. Enantioselective Hydrolysis of Racemic Styrene Oxide
and Its Substituted Derivatives Using Newly-Isolated Sphingopyxis Sp. Exhibiting a Novel Epoxide Hydrolase Activity. Biotechnol. Let., 2014, 36: 357-362 (30)
Lee E.Y., Shuler M.L. Molecular Engineering of Epoxide Hydrolase and Its
Application to Asymmetric and Enantioconvergent Hydrolysis. Biotechnol. Bioeng., 2007, 98: 318-327 (31)
Chen W.J.,
Lou W.Y. , Wang X.T., Zong M.H.. Asymmetric Hydrolysis of
Styrene Oxide Catalyzed by Mung Bean Epoxide Hydrolase in Organic Solvent/Buffer Biphasic System. Chinese J. Cat, 2011, 32: (32)
Botes A.L., Weijers C., van Dyk M.S. Biocatalytic Resolution of
1,2-Epoxyoctane Using Resting Cells of Different Yeast Strains with Novel Epoxide Hydrolase Activities. Biotechnol. Let., 1998, 20: 421-426 (33)
Krieg H.M., Botes A.L., Smith M.S., Breytenbach J.C., Keizer K. The
24 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Enantioselective Catalytic Hydrolysis of Racemic 1,2-Epoxyoctane in a Batch and a Continuous Process. J. Molecul. Cat. B-Enzym., 2001, 13: 37-47 (34)
Krieg H.M., Breytenbach J.C., Keizer K. Resolution of 1,2-Epoxyoctane by
Enantioselective Catalytic Hydrolysis in a Membrane Bioreactor. J. Mem. Sci., 2000, 180: 69-80 (35)
Chen W.J., Lou W.Y., Zong M.H. Efficient Asymmetric Hydrolysis of
Styrene Oxide Catalyzed by Mung Bean Epoxide Hydrolases in Ionic Liquid-Based Biphasic Systems. Bioresour Technol, 2012, 115: 58-62 (36)
Yu C.-Y., Li X.-F., Lou W.-Y., Zong M.-H. Cross-Linked Enzyme
Aggregates of Mung Bean Epoxide Hydrolases: A Highly Active, Stable and Recyclable Biocatalyst for Asymmetric Hydrolysis of Epoxides. J. Biotechnol., 2013, (37)
JU Xin P.J., XU Jianhe. Enantioconvergent Hydrolysis of P-Nitrostyrene
Oxide Catalyzed by Mung Bean Epoxide Hydrolase. Chinese J. Cat., 2008, 29: 696-700 (38)
Yu C.-Y., Wei P., Li X.-F., Zong M.-H., Lou W.-Y. Using Ionic Liquid in a
Biphasic System to Improve Asymmetric Hydrolysis of Styrene Oxide Catalyzed by Cross-Linked Enzyme Aggregates (Cleas) of Mung Bean Epoxide Hydrolases. Ind. Eng. Chem. Res., 2014, 53: 7923-7930 (39)
Abbott A.P., Capper G., Davies D.L., Rasheed R.K., Tambyrajah V. Novel
Solvent Properties of Choline Chloride/Urea Mixtures. Chem. Commun., 2003, 70-71 (40)
Durand E., Lecomte J., Baréa B., Piombo G., Dubreucq E., Villeneuve P.
Evaluation of Deep Eutectic Solvents as New Media for Candida Antarctica B Lipase Catalyzed Reactions. Process Biochem., 2012, 47: 2081-2089
25 ACS Paragon Plus Environment
Page 26 of 44
Page 27 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
(41)
Lindberg D., de la Fuente Revenga M., Widersten M. Deep Eutectic Solvents
(Dess) Are Viable Cosolvents for Enzyme-Catalyzed Epoxide Hydrolysis. J. Biotechnol., 2010, 147: 169-171 (42)
Kandiah M., Nilsen M.H., Usseglio S., Jakobsen S., Olsbye U., Tilset M.,
Larabi C., Quadrelli E.A., Bonino F., Lillerud K.P. Synthesis and Stability of Tagged Uio-66 Zr-Mofs. Chem. Mater., 2010, 22: 6632-6640 (43)
Cavka J.H., Jakobsen S., Olsbye U., Guillou N., Lamberti C., Bordiga S.,
Lillerud K.P. A New Zirconium Inorganic Building Brick Forming Metal Organic Frameworks with Exceptional Stability. J. Am. Chem. Soc., 2008, 130: 13850-13851 (44)
Blee E., Schuber F. Regio-and Enantioselectivity of Soybean Fatty Acid
Epoxide Hydrolase. J. Biolog. Chem., 1992, 267: 11881-11887 (45)
Sheldon R.A. Cross-Linked Enzyme Aggregates as Industrial Biocatalysts.
Org. Pro. Res. Dev., 2010, 15: 213-223 (46)
Hausdorf S., Wagler J.r., Moβig R., Mertens F.O. Proton and Water
Activity-Controlled Structure Formation in Zinc Carboxylate-Based Metal Organic Frameworks. J. Phys. Chem. A, 2008, 112: 7567-7576 (47)
Yang J., Dai Y., Zhu X., Wang Z., Li Y., Zhuang Q., Shi J., Gu J.
Metal–Organic Frameworks with Inherent Recognition Sites for Selective Phosphate Sensing through Their Coordination-Induced Fluorescence Enhancement Effect. J. Mater. Chem. A, 2015, 3: 7445-7452 (48)
Lei H., Wang W., Chen L.L., Li X.C., Yi B., Deng L. The Preparation and
Catalytically Active Characterization of Papain Immobilized on Magnetic Composite Microspheres. Enzyme and Microbial Technology, 2004, 35: 15-21
26 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
(49)
Talekar S., Ghodake V., Ghotage T., Rathod P., Deshmukh P., Nadar S.,
Mulla M., Ladole M. Novel Magnetic Cross-Linked Enzyme Aggregates (Magnetic Cleas) of Alpha Amylase. Bioresource Technol, 2012, 123: 542-547 (50)
Wang M., Qi W., Yu Q., Su R., He Z. Cross-Linking Enzyme Aggregates in
the Macropores of Silica Gel: A Practical and Efficient Method for Enzyme Stabilization. Biochem. Eng. J., 2010, 52: 168-174 (51)
Yu C.-Y., Li X.-F., Lou W.-Y., Zong M.-H. Cross-Linked Enzyme
Aggregates of Mung Bean Epoxide Hydrolases: A Highly Active, Stable and Recyclable Biocatalyst for Asymmetric Hydrolysis of Epoxides. J. Biotechnol., 2013, 166: 12-19 (52)
Lou W.-Y., Zong M.-H., Smith T.J., Wu H., Wang J.-F. Impact of Ionic
Liquids on Papain: An Investigation of Structure–Function Relationships. Green Chem., 2006, 8: 509-512 (53)
Vecchio G., Zambianchi F., Zacchetti P., Secundo F., Carrea G. Fourier‐
Transform Infrared Spectroscopy Study of Dehydrated Lipases from Candida Antarctica B and Pseudomonas Cepacia. Biotechnol. Bioeng., 1999, 64: 545-551 (54)
Zaks A., Klibanov A.M. Enzymatic Catalysis in Nonaqueous Solvents. J.
Biol. Chem., 1988, 263: 3194-3201 (55)
Klibanov A.M. Improving Enzymes by Using Them in Organic Solvents.
Nature, 2001, 409: 241-246 (56)
Danson M.J., Hough D.W. Structure, Function and Stability of Enzymes
from the Archaea. Trends Microbiol., 1998, 6: 307-314 (57)
Kumar V.V., Kumar M.P., Thiruvenkadaravi K., Baskaralingam P., Kumar 27 ACS Paragon Plus Environment
Page 28 of 44
Page 29 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
P.S., Sivanesan S. Preparation and Characterization of Porous Cross Linked Laccase Aggregates for the Decolorization of Triphenyl Methane and Reactive Dyes. Bioresour. Tech., 2012, 119: 28-34 (58)
Gorke
J.T.,
Srienc
F.,
Kazlauskas
R.J.
Hydrolase-Catalyzed
Biotransformations in Deep Eutectic Solvents. Chem. Commun., 2008, 1235-1237
28 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 30 of 44
Table of Contents Novel nano/micro-biocatalyst: soybean epoxide hydrolase immobilized on UiO-66-NH2 MOF Shi-Lin Cao, Dong-Mei Yue, Xue-Hui Li, Thomas J Smith, Ning Li, Hong Wu, Yong-Zheng Ma, Wen-Yong Lou*
Min-Hua Zong,
Preparation of the UiO-66-NH2 MOF and its efficient use for biocatalysis.
29 ACS Paragon Plus Environment
Page 31 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Figure Captions Scheme 1 Schematic illustration of the synthesis of the immobilization of SEH onto UiO-66-NH2. Scheme
Epoxide
2
hydrolase-catalysed
asymmetric
hydrolysis
of
UiO-66-NH2UiO-66-NH2
and
(R/S)-1,2-epoxyocatane to chiral (R)-1,2-octanediol. Figure
1
A,
macroscopic
appearance
of
SEH@UiO-66-NH2; B, SEM spectrum of SEH@UiO-66-NH2. Figure 2 FTIR analysis of UiO-66-NH2 MOFs, NH2-H2BDC, the N-H stretching of UiO-66-NH2 and the N-H stretching of H2N-H2BDC. Figure 3 The SEM graphs with high magnification of SEH@UiO-66-NH2 Figure 4 FTIR spectra of SEH and SEH@UiO-66-NH2. Figure 5 XRD of the UiO-66-NH2 (A1), the UiO-66-NH2 after treatment with PBS (A2), the UiO-66-NH2 after treatment with ChCl: Ethylene glycol (A3), the UiO-66-NH2 after treatment with ChCl: Xylitol (A4), the UiO-66-NH2 after treatment with ChCl: Glycerol (A5), the UiO-66-NH2 after treatment with ChCl: Urea (A6); XRD of the SEH@UiO-66-NH2 (B1), the SEH@UiO-66-NH2 after treatment with PBS (B2), the SEH@UiO-66-NH2 after treatment with ChCl: Ethylene glycol (B3), the
SEH@UiO-66-NH2
after
treatment
with
ChCl:
Xylitol
(B4),
the
SEH@UiO-66-NH2 after treatment with ChCl: Glycerol (B5), the SEH@UiO-66-NH2 after treatment with ChCl: Urea (B6). 30 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Figure 6 The effects of pH on the activity of free and immobilized enzymes. Figure 7 The effects of assay temperature on the activity of free and immobilized enzymes. Figure 8
pH stability of free and immobilized enzymes.
Figure 9 Thermal stability of free and immobilized enzymes. Figure 10 The amide I fitting results of free SEH and immobilized SEH via FTIR analysis. Figure 11 Time course of (R)-1, 2-octanediol with free and immobilized SEH in phosphate buffer (A) and immobilized SEH in various DESs containing system: ChCl: Urea(B), ChCl:Glycerol(C), ChCl:Ethanediol(D), ChCl:Xylitol(E).
31 ACS Paragon Plus Environment
Page 32 of 44
Page 33 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Scheme 1
Scheme 2
32 ACS Paragon Plus Environment
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Figure 1
33 ACS Paragon Plus Environment
Page 34 of 44
Page 35 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
N-H stretching of H2N-H2BDC
N-H stretching of UiO-66-NH2
v(NH2)sym
v(NH2)asym
v(NH2)sym
v(NH2)asym 3350
3400
3650 3600 3550 3500 3450 3400 3350 3300 3250
3450 -1
Wavenumber/cm-1
Wavenumber/cm
H2N-H2BDC
1656
1388
UiO-66-NH2
1800
1600
1400
1200
1000
800 -1
Wavenumber/cm Figure 2
34 ACS Paragon Plus Environment
600
400
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Figure 3
35 ACS Paragon Plus Environment
Page 36 of 44
Page 37 of 44
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
SEH@UiO-66-NH2
SEH
1800
1600
1400
1200
1000
800 -1
Wavenumber/cm Figure 4
36 ACS Paragon Plus Environment
600
400
10
Page 38 of 44
UiO-66-NH2 treated with ChCl:Urea
A6
UiO-66-NH2 treated with ChCl:Glycerol
A5
UiO-66-NH2 treated with ChCl : Xylitol
A4
UiO-66-NH2 treated with ChCl:Ethylene glycol
A3
UiO-66-NH2 treated with PBS
A2
UiO-66-NH2
A1
20
30
40
50
60
o
2 θ(
Relative Intensity
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Relative Intensity
ACS Sustainable Chemistry & Engineering
)
SEH@UiO-66-NH2 treated with ChCl:Urea
B6
SEH@UiO-66-NH2 treated with ChCl:Glycerol
B5
SEH@UiO-66-NH2 treated with ChCl : Xylitol
B4
SEH@UiO-66-NH2 treated with ChCl:Ethylene glycol
B3
SEH@UiO-66-NH2 treated with PBS
B2
SEH@UiO-66-NH2 10
20
B1 30
40
o
2 θ(
)
Figure 5 37
ACS Paragon Plus Environment
50
60
Page 39 of 44
20
Enzyme specific activity (U/mg SEH)
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
18 16 14 12 10 8
SEH@UiO66-NH2 Free SEH
6 6.0
6.5
7.0
7.5
8.0
pH Figure 6
38 ACS Paragon Plus Environment
8.5
ACS Sustainable Chemistry & Engineering
20
Enzyme specific activity (U/ mg SEH)
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 40 of 44
15
10 SEH@UIO-66NH2 Free SEH 5 25
30
35
40
45
Temperature/°C
Figure 7
39 ACS Paragon Plus Environment
50
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Enzyme specific activity (U/ mg SEH)
Page 41 of 44
16 SEH@UiO-66-NH2 Free SEH
14
12
10
6.0
6.5
7.0
7.5
pH Figure 8
40 ACS Paragon Plus Environment
8.0
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Enzyme specific activity (U/ mg SEH)
ACS Sustainable Chemistry & Engineering
18
Page 42 of 44
SEH@UiO-66NH2 Free SEH
16 14 12 10 8 6
20
25
30
35
40 o
Tenperature/ C Figure 9
41 ACS Paragon Plus Environment
45
100
0.25
90
0.20
80
0.15
60 50 40
SEH@UiO-66-NH2 α-Helix
0.10
β-Sheet
β-Turn
0.10
Intensity
70
0.15
Free SEH α-Helix
Intensity
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
ACS Sustainable Chemistry & Engineering
Secondary structure contents (%)
Page 43 of 44
β-Turn β-Sheet
0.05
0.05 0.00 1600
0.00
1620
1640 1660 -1 Wavenumber cm
1680
1700
1600
1620
1640 1660 -1 Wavenumber cm
Free SEH SEH@UiO-66-NH2
30 20 10 0 α-helix
β-sheet
β-turn
Assignment
Figure 10
42 ACS Paragon Plus Environment
1680
1700
ACS Sustainable Chemistry & Engineering
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Figure 11
43 ACS Paragon Plus Environment
Page 44 of 44