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Stabilization of lipase in polymerized high internal phase emulsions Stephanie M Andler, and Julie M Goddard J. Agric. Food Chem., Just Accepted Manuscript • Publication Date (Web): 27 Mar 2018 Downloaded from http://pubs.acs.org on March 27, 2018
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Stabilization of lipase in polymerized high internal phase emulsions Stephanie M. Andler and Julie M. Goddard* Department of Food Science, Cornell University, Ithaca, NY 14853.
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ABSTRACT
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Candida antarctica lipase B is stabilized in a porous, high internal phase emulsion (HIPE) of
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polydicyclopentadiene to enable biocatalytic waste stream upcycling. The immobilized lipase is
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subjected to thorough washing conditions and tested for stability in extreme environments and
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reusability. A porous internal microstructure is revealed through scanning electron microscopy.
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After preparation, lipase activity increased to 139±9.7% of its original activity. After ten cycles
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of reuse, immobilized lipase retains over 50% activity. Immobilized lipase retains activity after
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24 hours exposure to temperatures ranging from 20 ˚C to 60 ˚C, and pH values of 3, 7, and 10. In
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the most extreme environments tested, lipase retained 42.8±21 % relative activity after exposure
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to 60 ˚C, and 49.4±16% relative activity after exposure to pH 3. Polymerized HIPEs stabilize
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lipase, and thus extend its working range. Further synthesis optimization has the potential to
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increase enzyme stability, immobilization efficiency, and uniformity. The reported hierarchical
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stabilization technique shows promise for use of immobilized lipase in non-ideal, industrially
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relevant conditions.
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KEYWORDS: lipase, immobilization, enzyme, HIPE
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INTRODUCTION
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Industrial food processing waste streams represent a significant environmental burden, as an
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estimated 30-40% of all food is wasted.1–3 Enzymes have the potential to increase sustainability
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through the valorization of waste streams. Specifically, lipase B from Candida antarctica has
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been extensively studied for its ability to catalyze a variety of reactions with high specificity. 4,5
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For example, lipase can transform waste oil streams through esterification reactions,6 an important
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example of waste stream upcycling, as over 2 billion pounds of yellow grease were produced in
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the United States in 2015 alone.7 Lipase has been explored as a biocatalyst for biodiesel production
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from waste oil because of its specificity, lack of soap formation, and performance in the presence
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of interfering substances (e.g. free fatty acids, water).8–12 However, these esterification reactions
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typically require non-ideal conditions for native lipase (e.g. increased temperatures), which
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decrease activity and consequently reduce overall product conversion.13,14 Additionally, the cost
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of enzymes can be prohibitive to commercial adoption.
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To address these hurdles to commercialization, researchers have explored enzyme
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immobilization.15–17 The main methods to immobilize enzymes include binding to a carrier,
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entrapment and encapsulation, and cross-linking.17 The properties of the support material can
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influence the stability and activity of the enzyme; for example, pore size can impact diffusion of
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the substrate, thus influencing activity.18 Further, while in many cases a hydrophilic support is
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favored in retaining immobilized enzyme activity, many lipases are reported to undergo interfacial
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activation, in which the enzyme assumes an open, more active, form when situated at a
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hydrophobic interface.19–22 While not all sources of lipase exhibit interfacial activation,23–25
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hydrophobic materials are of interest for lipase immobilization.
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When considering the size and morphology of the solid support to which enzymes are
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immobilized, enzyme immobilization research has focused on either macroscale or nanoscale
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materials.15,26 While immobilization onto macroscale supports enables facile recovery, nanoscale
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immobilization can allow the enzyme to experience conditions similar to the native enzyme.
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However, as the size of the support decreases, the time for particle recovery increases.27 Thus,
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hierarchical structures, leveraging both nano- and macroscale materials, have gained interest
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because of their ability to leverage attributes from both orders of scale.26,28–30 Highly porous
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materials of appropriate pore size can present increased surface area for immobilization.18
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Importantly, these porous materials can be formed at macroscale sizes to permit facile handling
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and recovery.
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High internal phase emulsions (HIPEs) are porous structures, defined as having greater than 70%
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internal phase volume.31 Polymerized HIPEs have been produced from a variety of monomers
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including styrene, acrylates, methacrylates, and dicyclopentadiene.32–35 Few examples exist of
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enzyme containing HIPEs, which immobilize the enzyme after HIPE formation. 36,37 To our
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knowledge, no research exists on the incorporation of enzymes into the HIPE during
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polymerization.
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We have previously prepared cross-linked microparticles of polydicyclopentadiene with
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interfacially assembled nanoparticle-conjugated lipase.38–40
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mechanically robust polymer, produced from a ring opening metathesis polymerization.41,42 These
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~10 µM particles showed enhanced lipase stability across a wide range of pH values and
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temperatures, but were difficult to recover from viscous solvents.40 As a result, the present work
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synthesized lipase-containing macroscale polydicyclopentadiene HIPEs.
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Materials and Methods
Polydicyclopentadiene is a
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Materials
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Candida antarctica lipase B was kindly donated from c-LEcta (Leipzig, Germany). Resorufin
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butyrate was purchased from Santa Cruz Biotechnology (Dallas, TX, USA). Dicyclopentadiene,
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dimethylformamide (DMF), and toluene were purchased from Fisher Scientific (Fairlawn, NJ,
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USA). First generation Grubbs’ catalyst and Pluronic® L121 (poly(ethylene glycol)-block-
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poly(propylene glycol)-block-poly(ethylene glycol)) were purchased from Sigma-Aldrich (Saint
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Louis, MO, USA).
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High Internal Phase Emulsion (HIPE) Preparation
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HIPEs were fabricated using previously described methods, with modifications.34,35 The HIPE
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was prepared as 80% aqueous phase and 20% oil phase (v/v). Of the oil phase, 90% was Pluronic®
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L121 in dicyclopentadiene monomer (1% vol Pluronic® L121/vol monomer), and 10% Grubbs’
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catalyst (first generation) in toluene (5% wt Grubbs’ catalyst/vol toluene). For the aqueous phase,
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lipase was dissolved in 10 mM 2-(N-morpholino)ethanesulfonic acid (MES) buffer, pH 7 at a
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concentration of 50 µg protein/ml. Grubbs’ catalyst (first generation) was dissolved in toluene by
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sonicating for 10 minutes. Pluronic® L121 and dicyclopentadiene were blended for 5 minutes
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using magnetic stirring. Then, for the lipase containing samples, the lipase in MES buffer solution
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was added dropwise over 5 minutes. For the control HIPEs, 10 mM MES pH 7 was added
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dropwise over 5 minutes. The emulsion was then stirred for an additional two minutes. The
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solution of Grubbs’ catalyst was then added, and the emulsion was stirred for an additional two
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minutes. The emulsion was then poured into a three-cavity Teflon mold (21x 120mm, Ted Pella,
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Redding, CA, USA), and covered with embedding film (ACLAR Embedding Film 33C, Ted Pella,
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Redding, CA, USA). Embedding film covers were utilized to prevent shrinkage, which can occur
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upon rapid evaporation of the monomer.34
Polymerization was performed under ambient
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conditions (20 ˚C) to prevent denaturation of lipase. After 5 hours polymerization at 20 ˚C, the
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embedding film was removed, and HIPEs were dried overnight in the fume hood. The HIPEs
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were cut into 10 pieces per cavity, weighing approximately 30 mg each. HIPEs were washed in
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10 mM MES buffer, pH 7 for 5 cycles of 30 minutes at 20 ˚C.
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HIPE Activity
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HIPE activity was determined using the synthetic substrate 10 µM resorufin butyrate in pre-
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warmed 10 mM MES buffer pH 7, 50 ˚C. Resorufin butyrate was first dissolved in DMF at a
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concentration of 5.19 mM, then diluted to a final concentration of 10 µM in prewarmed 10 mM
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MES buffer pH 7. A piece of HIPE (approximately 30 mg) was placed in a 2 ml microcentrifuge
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tube. 600 µl of prewarmed substrate was added to the tube, and quickly vortexed before placing
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in a 50 ˚C incubator. The HIPEs were incubated for 3 minutes, then 300 µl was transferred to a
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black, 96-well plate. The samples were read using a plate reader (Synergy Neo 2, Biotek,
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Winooski, VT, USA) at 528/590 nm excitation and emission wavelengths, respectively. As a
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control, HIPEs prepared without lipase were tested for activity using the same procedure, and the
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fluorescence was subtracted from the HIPEs containing lipase.
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HIPE Washing Activity
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Freshly prepared HIPEs were washed for 5 cycles of 30 minutes at 20 ˚C in 10 mM MES buffer,
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pH 7. HIPEs were washed in a 50 ml centrifuge tube at a ratio of 1 mL buffer per ~30mg piece of
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HIPE. Tubes were rotated (Rotating Mixer R5010, Benchmark Scientific, Sayreville, NJ, USA)
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at 30 RPM. Following each wash cycle, four HIPEs were removed from the washing buffer, and
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tested for activity using the procedure described previously.
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HIPE Reuse
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Reuse of the HIPEs was determined by repeated exposure to the substrate, resorufin butyrate, and
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subsequent activity determination. Control and lipase containing HIPEs were tested for activity
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using the procedure described previously. After each exposure to the substrate, the HIPEs were
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washed 2 x 30 sec using 10 mM MES buffer, pH 7, then exposed to the substrate again. The
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process was repeated for a total of 10 cycles. Activity of subsequent cycles was compared relative
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to the activity of the first cycle.
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HIPE Thermostability
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Control and lipase containing HIPEs were first tested for activity using the procedure outlined
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previously. The HIPEs were then washed 2 x 30 sec in 10 mM MES buffer, pH7, then incubated
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at 20 ˚C, 40 ˚C, 50 ˚C, and 60 ˚C in 600 µl 10 mM MES buffer pH 7 for 24 hours. After 24 hours,
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the storage buffer was removed, and HIPE activity was tested according to the procedure outlined
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previously.
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incubation.
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HIPE pH Stability
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Control and lipase containing HIPEs were first tested for activity using the procedure outlined
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previously. The HIPEs were then washed 2 x 30 sec in 10 mM MES buffer, pH7, and incubated
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at pH 3, 7, and 10 in 600 µl 10 mM citrate, phosphate, and carbonate buffers, respectively, for 24
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hours at 20 ˚C. After 24 hours, the storage buffer was removed and HIPEs were washed with 0.1
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M MES buffer, pH 7. Then, activity was tested according to the procedure outlined previously.
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Activity of each HIPE was compared to its starting activity prior to incubation.
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Scanning Electron Microscopy
Activity of each HIPE was compared to its individual starting activity prior to
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Scanning electron micrographs were obtained using a benchtop SEM (JEOL Neoscope JCM 6000)
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operating at 15 kV (Nikon Instruments, Inc. Melville, NY).
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(Cressington Sputter Coater 108auto, Watford, UK) with gold prior to analysis. The reported
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image is representative of 9 images acquired across each of two independently prepared samples.
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Statistical Analysis
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All experiments were performed using n=4 samples, and repeated on a second day, using
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independently prepared HIPEs. HIPEs were synthesized in the absence of lipase and used as a
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negative control for all experiments. Statistical analysis was performed using Graphpad
Samples were sputter coated
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Prism software (v. 7.01, GraphPad Software, La Jolla, CA). All experimental data were treated
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as paired data. For Washing Activity, Thermostability, and pH Stability experiments, one-way
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analysis of variance (ANOVA) with Tukey’s pairwise comparison for the identification of
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statistical differences was performed using p < 0.05. For Reuse experiments, One-way analysis
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of variance (ANOVA) with Dunnet’s pairwise comparison for the identification of statistical
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differences was performed using p < 0.05.
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RESULTS AND DISCUSSION
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HIPE synthesis overcomes some hurdles to commercial adoption of immobilized enzymes, as
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only mixers and casting molds are needed, and synthesis can be readily scaled up. Scanning
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electron microscopy (SEM) (Figure 1) revealed a porous internal microstructure, confirming
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successful formation of the polymerized HIPEs and the presence of a hierarchical structure. This
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porosity provided a high surface area amenable for protein loading. Initial activity of as-prepared
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HIPEs revealed approximately 139±9.7% activity retention compared to native lipase. However,
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lipase was not strongly immobilized, as shown by a decrease in relative activity (as compared to
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as-prepared HIPE activity) with each subsequent wash cycle (Figure 2). Following an initial
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decrease, relative activity stabilized after the fourth wash, representing activity of immobilized
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lipase. The observed decrease in activity suggests loss of lipase from weak immobilization,
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possibly a result of the surface-active nature of the surfactant, which may have competed with
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lipase for sites in interfacial assembly. To ensure subsequent tests evaluated only immobilized
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lipase, stability and reuse experiments used HIPEs that had undergone the 5-cycle washing step.
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Reported values represent the mean of n=4 samples, with error bars representing standard
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deviation, and are representative of experiments repeated on two days, with independently
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prepared HIPEs.
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The performance of the immobilized lipase HIPEs under conditions of pH and temperature
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extremes was determined to characterize efficacy under industrially relevant conditions. To
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determine HIPE stability in varying pH environments, HIPEs were tested for initial activity, then
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washed and stored in pH 3, 7, and 10 buffers for 24 hours at 20 ˚C (Figure 3). After storage at pH
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3, HIPEs retained 49.4±16% activity. This activity retention is an improvement over native lipase,
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which has been shown to lose almost all activity at pH 3.39 At pH 7, HIPEs retained 76.7±7%
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activity, suggesting favorable working conditions at neutral pH. At pH 10, HIPEs retained
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62.7±5% activity, showing that immobilization within polydicyclopentadiene broadens the
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working range of lipase. We hypothesize that the polydicyclopentadiene is providing stability to
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the structure of lipase, and possibly influences the microenvironment that lipase experiences. 40
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The observed decrease in activity across all pH values may also be attributed to weak
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immobilization and migration of the enzyme.
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To determine thermostability of immobilized lipase, HIPEs were tested for activity, washed, and
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stored in 10 mM MES buffer (pH 7) at 20 ˚C, 40 ˚C, 50 ˚C, and 60 ˚C for 24 hours. After exposure,
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HIPEs retained 111.6±23, 157.5±21, 54.0±19, 42.8±21 % activity at 20 ˚C, 40 ˚C, 50 ˚C, and 60
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˚C, respectively (Figure 4). At 20 ˚C and 40 ˚C, HIPEs showed an increase in activity compared
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to their starting activity. These data further support that stabilizing interactions occur between
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polydicyclopentadiene and lipase. HIPEs retained activity after storage at 50 ˚C and 60 ˚C, in
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contrast to native lipase which has been reported to lose all activity at elevated temperatures within
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approximately 2 hours, and Novozym 435, which loses greater than 60% activity at 60 ˚C.39
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Elevated temperatures are commonly required for esterification reactions, supporting the need for
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stabilized enzymes. These data further support the use of polydicyclopentadiene as a support
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material for lipase in extreme environments.
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Because enzymes are more expensive than their chemical counterparts, reusability is imperative
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for commercial adoption. For proof of concept, HIPEs were exposed to the resorufin butyrate for
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total of 10 cycles, with washes (10 mM MES buffer, pH 7) between cycles. Activity was
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monitored after each cycle and compared to the starting activity.
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activity after each reuse cycle. HIPEs retained over 50% activity after 10 cycles, showing promise
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for reusability.
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significant, could point towards improvement in the post-polymerization washing process.
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Additionally, concentrations of both protein and surfactant can be optimized to support lipase
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interfacial assembly. These results are in agreement with practical application of Novozym 435
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to hydrolysis of waste cooking oil, where 62% activity remained after 4 cycles of reuse. 43
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Nevertheless, the sustained activity over 10 cycles suggests potential for reuse.
Figure 5 shows average HIPE
The initial observed drop in activity (63.9±9.5%), while not statistically
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These results show the potential for use of hierarchical materials as solid supports in the
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stabilization of enzymes for industrial waste reutilization processes. Immobilized lipase was
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stabilized in polymerized HIPEs and retained activity after exposure to non-ideal environments,
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retaining approximately 49% activity at pH 3 and approximately 42% activity at 60 ˚C after 24
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hours exposure. Further research is necessary to determine stability in practical solvents and
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further in practical applications; however, the tailorable size of the HIPE makes the process
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suitable for scale-up and customization. HIPE synthesis optimization may further improve lipase
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stability; for example, manipulating protein concentration, mixing shear, aqueous phase percent,
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and surfactant type.
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immobilization and offer advantages over free enzymes. Enzymatic valorization of waste streams
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can eliminate the need for toxic solvents and reduce the formation of by-products.
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optimization, lipases immobilized in polymerized HIPEs can be considered for industrial
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esterification reactions. Further, the value-added reutilization of waste streams, and greener
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processing methods can help improve the environmental sustainability of industrial food
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manufacturing.
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AUTHOR INFORMATION
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Corresponding Author
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*
[email protected]. * Department of Food Science, Cornell University, Ithaca, NY 14853
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Author Contributions
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The manuscript was written through contributions of all authors. All authors have given approval
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to the final version of the manuscript.
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Notes
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There are no conflicts to declare.
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ACKNOWLEDGMENT
Nevertheless, hierarchical structures show promise for enzyme
With further
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This project was supported, in part, by the USDA Agriculture and Food Research Initiative Grant
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no. 2014-67021-21584, and the Cornell Institute for Food Systems Industry Partnership Program.
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ABBREVIATIONS
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HIPE, high internal phase emulsion; MES, 2-(N-morpholino)ethanesulfonic acid; SEM, scanning electron microscopy.
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Properties of HIPE Templated Macroporous Poly(Dicyclopentadiene) Prepared with Low
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Surfactant Amounts. J Mater Chem A 2013, 1 (3), 487–490.
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FIGURE CAPTIONS
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Figure 1. SEM micrograph of cross-section of HIPE. A highly porous network is formed though
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the polymerization of the monomer.
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Figure 2. Relative percent activity of HIPEs after each 30-minute was with 10 mM MES buffer,
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pH 7. Relative activity was determined using resorufin butyrate and was calculated by comparison
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to the starting activity of unwashed HIPEs. Values represent means of n=4 determinations with
341
error bars representing standard deviation.
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Figure 3. Activity of HIPEs after exposure to pH 3, 7, 10 for 24 hours. Relative activity was
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determined using resorufin butyrate and compared to the starting activity of each HIPE after
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washing. Values represent means of n=4 determinations with error bars representing standard
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deviation.
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Figure 4. Activity of HIPEs after 24 hours exposure to 20 ˚C, 40 ˚C, 50 ˚C, and 60 ˚C. Activity
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was determined using resorufin butyrate and compared to the starting activity of each HIPE.
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Values represent means of n=4 determinations with error bars representing standard deviation.
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Figure 5. Activity of HIPEs after exposure to resorufin butyrate for a total of 10 cycles. Over
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50% activity is retained after 10 cycles of reuse. Values represent means of n=4 determinations
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with error bars representing standard deviation.
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FIGURE GRAPHICS Figure 1
Figure 2
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Figure 3
Figure 4
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Figure 5
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GRAPHIC FOR TABLE OF CONTENTS
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