Joachim C.
Lentz
a,
Robert
Cavanagh
b,
Cara
Moloney
b,
Bruno
Falcone Pin
a,
Kristoffer
Kortsen
a,
Harriet R.
Fowler
a,
Philippa L.
Jacob
a,
Eduards
Krumins
a,
Charlotte
Clark
a,
Fabricio
Machado
ad,
Nicholas
Breitkreuz
a,
Ben
Cale
c,
Amy R.
Goddard
c,
Jonathan D.
Hirst
a,
Vincenzo
Taresco
*a and
Steven M.
Howdle
*a
aSchool of Chemistry, University of Nottingham, University Park, NG7 2RD, Nottingham, UK. E-mail: vincenzo.taresco@nottingham.ac.uk; steve.howdle@nottingham.ac.uk
bSchool of Pharmacy, University of Nottingham, University Park, NG7 2RD, Nottingham, UK
cCroda Europe Limited, Cowick Hall, Snaith, DN14 9AA, Goole, UK
dInstitute of Chemistry, University of Brasília, Campus Universitário Darcy Ribeiro, 70910-900, Brasília, DF, Brazil
First published on 10th October 2022
N-Hydroxyethyl acrylamide was used as a functional initiator for the enzymatic ring-opening polymerisation of ε-caprolactone and δ-valerolactone. N-Hydroxyethyl acrylamide was found not to undergo self-reaction in the presence of Lipase B from Candida antarctica under the reaction conditions employed. By contrast, this is a major problem for 2-hydroxyethyl methacrylate and 2-hydroxyethyl acrylate which both show significant transesterification issues leading to unwanted branching and cross-linking. Surprisingly, N-hydroxyethyl acrylamide did not react fully during enzymatic ring-opening polymerisation. Computational docking studies helped us understand that the initiated polymer chains have a higher affinity for the enzyme active site than the initiator alone, leading to polymer propagation proceeding at a faster rate than polymer initiation leading to incomplete initiator consumption. Hydroxyl end group fidelity was confirmed by organocatalytic chain extension with lactide. N-Hydroxyethyl acrylamide initiated polycaprolactones were free-radical copolymerised with PEGMA to produce a small set of amphiphilic copolymers. The amphiphilic polymers were shown to self-assemble into nanoparticles, and to display low cytotoxicity in 2D in vitro experiments. To increase the green credentials of the synthetic strategies, all reactions were carried out in 2-methyl tetrahydrofuran, a solvent derived from renewable resources and an alternative for the more traditionally used fossil-based solvents tetrahydrofuran, dichloromethane, and toluene.
Ring-opening polymerisation (ROP) allows for the synthesis of aliphatic polyesters through cyclic monomers such as lactide, lactones (e.g. caprolactone, β-propiolactone, γ-butyrolactone, δ-valerolactone, ε-caprolactone), among others.3 Relief of ring-strain rather than removal of condensate allows ROP to take place under milder conditions than those required for polycondensation.7 Milder conditions facilitate the use of thermally sensitive monomers as well as limiting discolouration and degradation during synthesis.8 Furthermore, by addition of an initiator in ROP, a variety of end-groups can be installed.9 The presence of an initiator also allows control over targeted molecular weight by varying the ratio of initiator to monomer.10 Functional ROP initiators provide a straightforward pathway to produce aliphatic polyesters that can be further derivatized post-polymerisation. 2-Hydroxyethyl methacrylate (HEMA) is a well-studied example of one such functional initiator, since it contains both a primary hydroxyl and a methacrylic group.1,5,6,11–13 HEMA has been used as ROP initiator for enzymatic, metal-based, and organocatalytic routes.1,14
A large portion of published research on these functional ROP systems features tin(II) 2-ethylhexanoate as catalyst.2,3 Drawbacks of these systems include difficulty of removing tin residues during purification; particularly important for biomedical devices.1,15,16 Furthermore, these catalysts exhibit high toxicity towards mouse fibroblasts and human endothelial cells fibroblasts.17
Enzymatic catalysis is a viable metal-free alternative to produce polymers by ROP (eROP).3,15,18 Using an enzyme that is both commercially available and immobilized overcomes a plethora of issues traditionally associated with enzymatic and organo-catalysis.19 Commercial availability removes the need for in-house enzyme purification and production expertise. Enzyme immobilization can be used to improve stability, activity, and selectivity.19,20 In this context however, the improved chemical resistance, recyclability, and ease of handling are the greatest benefits of immobilisation.19,20 Lipase B from Candida antarctica (CALB), which has been extensively studied for eROP and enzymatic polycondensation, is commercially available in an immobilized formulation under the name Novozym 435 (N435).3,15,21
Novozym 435 catalysed ROP, using HEMA or other ester containing molecules as ROP initiators, has been limited by a lack of differentiation between the ester bond in the initiator and the ester bond in the monomer.5 Further radical polymerisation techniques are made impossible by transesterification, since the ethylene glycol dimethacrylate that is formed will act as a cross-linker yielding insoluble material. In addition, the ethylene glycol, produced as a by-product, can act as an eROP initiator – producing chains lacking the desired end group functionality (ESI Fig. 1†). The lack of selectivity leads to methacrylate and polyester transfers in eROP.5,6,22 Takwa et al.5 used HEMA initiated eROP followed by addition of vinyl methacrylate to create a series of biodegradable cross-linkers. However, for the synthesis of unbranched polymers, transesterification severely limits the use of acrylates as initiators in eROP. To initiate eROP whilst maintaining control over the end-groups, it is imperative that the initiator is stable in the presence of the enzyme.
To overcome issues of transesterification associated with methacrylate and acrylate based initiators, in the present work, we considered acrylamides as alternative ROP initiators. Since the amide bond exhibits greater stability towards nucleophilic attack, it was thought that a serine-based lipase such as CaLB relying on an initial nucleophilic attack would be unable to catalyse self-reaction (Fig. 1B) in the working conditions employed.3N-Hydroxyethyl acrylamide (HEAA) was identified as a potential alternative to HEMA due to its analogous structure, low cost, and commercial availability. Like HEMA, HEAA contains both a primary hydroxyl as well as a radically polymerisable group. HEAA has been widely utilized in coatings, sealants, thermosetting paints, and personal care products.23 Poly(HEAA) has strong anti-fouling properties,24 and has received particular interest as a material for protein separation,25 and drug delivery systems.26,27
Fig. 1 A: transesterification of HEMA in the presence of N435 leads to cross-linkers and diols capable of acting as bifunctional eROP initiators which lead to the formation of mono-methacrylate, di-methacrylate, and non-methacrylated poly(caprolactone) products, seen in ESI Fig. 1.† B: HEAA however, is hypothesised not to undergo analogous reactions in the presence of N435. |
Motivated by the properties of HEAA that make its use in biomaterials advantageous, this paper investigates the use of HEAA as a functional eROP initiator for nanoparticle (NP) formulation. The stability of HEAA was confirmed in the presence of N435, and so HEAA was investigated as an eROP initiator for both caprolactone (CL) and valerolactone (VL), according to the reaction scheme show in Fig. 2.
Both HEAA-PCL and HEAA-PVL contain an acrylamide end-group, which is in principle available for radical polymerisation post eROP. Radical co-polymerisation can be used to tune hydrophilicity by introduction of water-soluble co-monomers. Tuning the hydrophilicity should allow control over the size and stability of NPs produced. The presence of a degradable aliphatic polyester should also allow excretion of the NPs, thereby avoiding bioaccumulation.28
Dichloromethane (DCM) and tetrahydrofuran (THF) are solvents routinely used for a variety of polymerisation processes, owing to their excellent solubility parameters, they are unfortunately derived from petrochemical feedstocks. DCM is also known to be carcinogenic and contribute to ozone layer depletion.29 In order to avoid using petroleum derived chemicals alternatives are required. 2-Methyl tetrahydrofuran (2-MeTHF) is a bio-based solvent, produced from chemical and enzymatic treatment of biomass, and has similar solubility parameters to petrochemical solvents.30–32 In addition, it possesses a relatively high boiling point (80 °C), and a lower critical solution temperature with water than THF – crucial for limiting hydrolytic initiation of ROP. Furthermore, the cost of 2-MeTHF on a lab-scale is comparable to that of non-renewable solvents. Previous work in the group has demonstrated the suitability of 2-MeTHF as a solvent for multi-polymerisations combining eROP with both free-radical and reversible addition–fragmentation chain transfer (RAFT) polymerisation.4
In this paper we report the use of HEAA as a functional initiator in eROP, and subsequent Free-Radical Polymerisation (FRP) of the produced macromonomers. HEAA initiated eROP was studied in-depth by 1H-NMR spectroscopy and incomplete initiator conversion was observed. Computational docking studies were employed to gain insight into the cause of incomplete initiator conversion. End-group fidelity of the materials was demonstrated by chain extension using the organocatalyzed ROP of lactide, as well as radical (co-)polymerisation. The materials were shown to be non-toxic through in vitro tests against lung, intestinal, and skin cells. Amphiphilic co-polymers of HEAA-PCL and PEGMA were assembled into polymeric NPs by nanoprecipitation.
It should be noted that HEAA, unlike HEMA, is associated with Hazard Statement H373 “May cause organ damage through prolonged or repeated exposure”. This is for the monomers. However once polymerised, neither the eROP synthesised macroinitiator nor the related FRP synthesised homo and (co-)polymers showed any relevant cytotoxicity in the in vitro experiments performed (see Cytotoxicity measurements Fig. 10).
The lack of reactivity of HEAA towards itself in the presence of N435 is a strong indication that the amide bond in HEAA is stable under the reaction conditions employed during eROP. The extra stability of HEAA over HEMA can be explained by the lower electronegativity of nitrogen compared to that of oxygen, leading to greater delocalisation of the nitrogen lone pair into the carbonyl bond.34,35 As a result, the carbonyl oxygen resonance hybrid already holds a more significant partial negative charge decreasing its susceptibility towards nucleophilic attack.
Candida antarctica Lipase B (CALB), the active enzyme in N435, catalyses esterification via an initial nucleophilic attack of the carbonyl bond by an activated serine residue in its active site.36 It was hypothesised that the initial nucleophilic attack of the catalytic cycle might be inhibited by the decrease in electrophilicity going from an ester to an amide (ESI Fig. 5†).
The stability of the initiator is vital to enable synthesis of HEAA initiated ROP products whilst maintaining control over the end groups. The promising results (ESI Fig. 3 and Table 1†) gave us confidence that HEAA is suitable as an eROP initiator, and CL and VL were selected to be the model monomers for HEAA initiated eROP using N435.
HEAA initiated eROP of CL (1:20 I:M) was also monitored by GPC. From the chromatograms polymer growth and oligomeric materials can be observed. These oligomers were removed by precipitation into methanol (Fig. 8). However, unimodality is observed in the main polymer peak, suggesting a single species is forming. Molecular weight predicted by 1H-NMR and GPC are in good agreement, when partial conversion of HEAA is considered during molecular weight calculation (eqn (S5)†). When HEAA conversion is not considered molecular weight is significantly underestimated (ESI Table 2†). Discrepancies between molecular weight between GPC and 1H-NMR spectroscopy can arise from the GPC being calibrated to PMMA standards, which have different hydrodynamic volume compared to PCL.38 Furthermore, 1H-NMR does not have a lower limit of calibration, unlike GPC, resulting in oligomers being considered into the estimated molecular weight. Oligomers will be below the lower limit of calibration by GPC (around 800 Da), leading to overestimation of molecular weight in comparison to 1H-NMR (Fig. 4, left). Dispersity increases over time (ESI Table 2†), potentially due to transesterification taking place during polymerisation, although remains reasonably low (Đ = 1.28 at 30 min, to Đ = 1.51 at 300 min) (Fig. 4, right).
MALDI-TOF mass spectroscopy was performed on a sample of HEAA-PCL after purification by precipitation (ESI Fig. 10†). The obtained mass spectrum shows species with Na+ and K+ counterions (m/z difference of 16) but very clearly there is just a single polymer species observed. Difference in m/z of 114 between each additional unit correlating excellently with addition of single monomer units of caprolactone. Unfortunately, end-groups could not be accurately determined from MALDI alone. Mass determined by 1H-NMR end-group analysis (1797 g mol−1) and by MALDI (most intense peak 2104.5 m/z) are in close agreement, indicating that the primary species present is HEAA initiated PCL. However, as seen from the control experiments performed, residual water bound to N435 is also capable of acting as an initiator. Therefore, the presence of water-initiated chains cannot be excluded and is a limitation of the reaction methodology.
Turnover frequency for these reactions was calculated (ESI Table 4†) using literature methodology.39 Turnover frequencies are significantly higher in the initial stages of reaction. From the recyclability study (see ESI†) it can be ascertained that this decrease in turnover frequency is not a result of the enzyme losing catalytic activity. The decrease in turnover frequency is instead an effect of monomer concentration decreasing during reaction. An enzyme recyclability study was also performed (see ESI†). No loss in reactivity was observed over ten reaction cycles, demonstrating the robustness of the catalyst in the reaction conditions employed. Lactone and initiator conversion were consistent throughout the reaction cycles.
Control experiments without enzyme (reaction vessel containing HEAA and CL) and without HEAA (reaction vessel containing CL and N435) as initiator were also performed. No polymerisation of CL into PCL was observed upon removal of N435 (ESI Table 11†). On the other hand, upon removal of HEAA, polymerisation was observed between CL and N435. The polymerisation onset is likely due to residual water bound to the enzyme, as reported by previous literature.40,41 This background polymerisation proceeds significantly slower than when the HEAA initiator is added, and results in polymers of significantly higher dispersity. By GPC, polymer could only be detected after 2 hours of reaction, whereas when HEAA is added significant yield is seen within 30 minutes (ESI Fig. 11, and Table 5†). Whilst secondary initiation processes could not be removed entirely, the increased rate of reaction and the decreased dispersity can certainly be attributed to the presence of the desired initiator.
The natural logarithm of PCL and PVL formation were plotted against time to obtain a linear trend (Fig. 5). HEAA was used as an internal 1H-NMR standard to determine relative polymer concentration at sampling times, a more in-depth explanation and tabulated results can be found in the ESI† under the subsection “Plotting First-Order Kinetics”. Rate of reaction was found to be proportional to the concentration of lactone present, following first-order kinetics. VL does not appear to follow first order kinetics as closely as CL. For VL, the data points corresponding to 240 and 300 minutes were excluded, as the kinetics deviate from first-order kinetics as the reaction reaches equilibrium. R2 values exceed 0.95 when considering the first 180 minutes of reaction, indicating an adherence to first order kinetics for the initial stages of reaction. From conversion of the lactones into their respective poly(lactone)s it appears that this reaction proceeds following first order kinetics with respect to the lactone monomer. A deeper kinetic analysis contained in the ESI† enabled us to clarify in more detail the reactivity of VL and CL. VL was found to have significantly lower kinetic constants than CL, and to deviate from first-order kinetics (more details can be found in the section “Deeper Kinetics Analysis” in the ESI†).
Purification was achieved by precipitation into methanol or diethyl ether, confirming that the increase in 1H-NMR signals is due to unreacted initiator rather than initiator degradation or self-reaction (ESI Fig. 9†). No extra peaks related to side products (i.e. ethanolamine, ESI Fig. 4†) were detected. In contrast, HEMA initiated eROP suffers from the targeted product and side products having almost identical solubility characteristics, and as a result purification by precipitation is impossible (ESI Fig. 1†).5
It was possible to calculate the extent of initiator conversion using the two double doublets between 6.31 and 6.25 ppm corresponding to protons A and 1 (ESI Fig. 6 and 7†). Initiator consumption versus time is plotted in Fig. 6.
HEAA reaches conversions significantly lower than the conversions observed for CL and VL. As a result, targeted DP is exceeded, and unreacted HEAA can be found in the reaction mixture. As longer chains are targeted greater initiator conversion is observed. This is thought to be an effect of lowered reactivity as the poly(lactone) chain grows, due to increased steric hindrance.
It was hypothesised that chains of HEAA-PCL and HEAA-PVL are better substrates for N435 than HEAA, and therefore react faster than HEAA. The higher rate of monomer consumption by growing chains would in turn lead to complete monomer conversion before complete initiator conversion has been achieved. To further understand this phenomenon, HEAA and HEAA-CL were docked into the N435 active site using computational methods.
From GBSA computed interaction energies, HEAA-CL binds approximately twice as strongly as HEAA. Based on the Autodock scores the difference is less pronounced, but HEAA-CL still exhibits a greater binding affinity to CALB than HEAA. Autodock scores and GBSA energies are obtained through different methods. Although the absolute values are not directly comparable, the trends between the compounds are of interest to gauge relative binding affinity to the enzyme active site.
To grow a poly(lactone) chain using N435, the activated monomer unit needs to be released from the acyl-enzyme intermediate in the rate-determining step. The release of monomer and regeneration of the enzyme occurs through nucleophilic attack by either an initiator or a propagating chain (ESI Fig. 17†).36 The rate of reaction is highly dependent on the binding interactions between enzyme and substrate.42 The higher affinity of HEAA-CL towards CaLB compared to HEAA rationalises the experimental results observed during eROP. Since HEAA-CL has a higher binding affinity than HEAA, it is more likely to be found in the enzyme active site and will subsequently react at a faster rate than HEAA. As a result, reactions involving propagating chain proceed at a faster rate than initiation, yielding unreacted initiator when all monomer has been consumed.
To obtain complete initiator conversion, the initiator should react at a faster rate than the propagating chains. To achieve rapid initiation an alternative initiator species that is more reactive in the presence of N435 could be used (HEMAM was screened, see “Alternative Initiator Species” in the ESI†), alternatively the enzyme active site could be modified to improve the suitability of HEAA as substrate although this is beyond the scope of the current work.
Fig. 8 (A) Reaction scheme of HEAA-PCL extension with lactide using DBU. (B) 1H-NMR spectra of time zero and after 30 minutes, zoomed to 5.05–5.25 ppm – full spectra in ESI Fig. 18.† Peak marked with * is a DCM satellite. (C) GPC traces of HEAA-PCL (GPC Mn 9.45 kDa, Đ 1.2, 1H-NMR 4.5 kDa) and HEAA-PCL-PLA (GPC Mn 19.4 kDa, Đ 1.2, 1H-NMR 43 kDa) demonstrating a single polymer peak in both chromatograms. |
In order to produce an A–B (A: PCL, B: PLA) block copolymer, we exploited the stability of the first block (HEAA-PCL) polymer and the compatibility of DBU with HEAA and 2-MeTHF. Lactide was added in a ratio of 300:1 with respect to HEAA-PCL and allowed to react for 30 minutes. The organocatalyzed ROP was monitored by 1H-NMR spectroscopy. Ring-opening of lactide is monitored using the peaks at 5.05 (quartet) and 5.25 ppm (broad multiplet) corresponding to monomeric lactide and polymeric PDLLA respectively. Conversion was found to be approximately 98% by 1H-NMR analysis. The successful chain extension and subsequent formation of a blocky system was confirmed by the presence of one single peak in the GPC chromatogram (with increased final number average molecular mass). Furthermore, chain extension of PCL with lactide leads to opportunities for tuneable biodegradability to the materials.
Fig. 9 Synthetic strategy for the co-polymerisation of HEAA-PCL with PEGMA and subsequent nanoprecipitation into water. |
PEGMA was chosen as the hydrophilic co-monomer due to its excellent biocompatibility,44,45 and widespread use in NP formation for drug delivery applications.46,47 Presence of a hydrophilic moiety such as PEGMA stabilized the NPs formed in aqueous media. FRP of a non-precipitated sample of HEAA-PCL (i.e. also containing unreacted HEAA due to incomplete initiator consumption observed) demonstrated an enhanced ability to assemble into NPs thanks to the hydrophilic HEAA present. Suitability of HEAA as a hydrophilic co-monomer removes the need for precipitation after eROP, improving the green credentials of the reaction by limiting purification steps and solvent requirements.
Significant discrepancies between molecular weight values (expected versus those measured by GPC) were observed for the FRP products. These effects are likely due to significant chemical differences between synthesised amphiphilic materials and the PMMA standards used for calibration. This has been previously described in literature38 and might be a result of different solvated volumes and column-polymer interactions (Table 2).
Polymer | Ratio (HEAA-PCL):comonomer | Conversiona (%) | M n GPCb (kDa) | M w GPCb (kDa) | Đ |
---|---|---|---|---|---|
a Determined by 1H-NMR spectroscopy deemed quantitative when no olefinic protons visible in the spectrum. b Determined by GPC in THF. | |||||
Poly-(HEAA-PCL)44 | 1:0 | Quant. | 14.1 | 21.9 | 1.6 |
(HEAA-PCL)44-co-PEGMA | 4:6 | 99 | 5.39 | 9.66 | 1.8 |
(HEAA-PCL)44-co-PEGMA | 7:3 | 94 | 11.2 | 15.8 | 1.4 |
Poly-(HEAA-PCL)15 | 1:0 | Quant. | 9.18 | 13.2 | 1.4 |
(HEAA-PCL)15-co-PEGMA | 4:6 | 98 | 4.00 | 5.36 | 1.3 |
(HEAA-PCL)15-co-PEGMA | 7:3 | 99 | 5.71 | 8.87 | 1.6 |
(HEAA-PCL)10-co-HEAA | Approx. 1.80:0.17 | Quant. | 8.90 | 15.4 | 1.7 |
Entry | Polymer | Ratio (HEAA-PCL):comonomer (mass:mass) | Hydrodynamic diameter (nm) | PDI |
---|---|---|---|---|
DLS measurements were performed in deionised water at a concentration of 1 mg mL−1. | ||||
1 | (HEAA-PCL)44-co-PEGMA | 4:6 | 104.3 ± 1.2 | 0.189 ± 0.005 |
2 | (HEAA-PCL)44-co-PEGMA | 7:3 | 107.6 ± 1.1 | 0.213 ± 0.001 |
3 | (HEAA-PCL)15-co-PEGMA | 4:6 | 120.2 ± 4.4 | 0.556 ± 0.039 |
4 | (HEAA-PCL)15-co-PEGMA | 7:3 | 141.1 ± 0.8 | 0.483 ± 0.004 |
5 | (HEAA-PCL)10-co-HEAA | Approx. 1.80:0.17 | 310.8 ± 3.5 | 0.235 ± 0.005 |
HEAA-PCL was carried forward to produce amphiphilic graft copolymers. As a proof of concept of a simple and largely adopted class of reaction, FRP with PEGMA as a co-monomer was performed. This FRP co-polymerisation yielded materials that were capable of self-assembly into NPs, whereas purely hydrophobic homopolymers only yielded poorly defined aggregates. One-pot eROP and subsequent FRP of crude HEAA-PCL, still containing unreacted and hydrophilic HEAA, also yielded material capable of self-assembly into NPs. The ability of unreacted HEAA to aid in NP formation can be exploited to carry out eROP and subsequent FRP in one-pot, minimizing synthetic steps and solvent use. Materials were assayed for cytotoxicity against three model cell lines (Caco-2, A549, and A431) to determine their viability for application in biological context, and found to be non-toxic at concentrations up to 500 μg mL−1.
For the enzyme recyclability study, the same procedure as above was followed, where the Novozym 435 was collected and re-used.
For the control experiments, the same procedure as above was followed, excluding addition of initiator.
The lactate dehydrogenase (LDH) release assay (Sigma Aldrich, TOX7 kit) and PrestoBlue cell viability assay (Thermo Fisher Scientific) were performed to assess cytotoxicity. Cells were seeded at 1.2 × 105 cells per well in 12 well plates and cultured for 24 hours prior to assaying. Polymeric materials were exposed to cells at 500 μg mL−1 for 48 hours and applied in 1 mL phenol red free DMEM containing 10% (v/v) FBS and 2 mM L-glutamine. Triton X-100 (TX) applied at 1% (v/v) applied in phenol red free medium was used as a cell death (positive) control and a vehicle control containing no polymeric material used as a negative control. Following exposure, sample supernatant was collected from wells for analysis of LDH content. Cells were then washed twice with warm PBS and 10% (v/v) PrestoBlue reagent diluted in phenol red free medium applied per well for 60 minutes. The resulting fluorescence was measured at 560/600 nm (λex/λem). Relative metabolic activity was calculated by setting values from the negative control as 100% and positive control values as 0% metabolic activity. Assessment of LDH release was performed according to the manufacturer's instructions and involved adding LDH reagent to collected supernatant samples and incubating at room temperature shielded from light for 25 minutes. Absorbance was then measured at 492 nm. Relative LDH release was calculated with the negative control absorbance at 492 nm taken as 0%, and the positive control, assumed to cause total cell lysis, as 100%.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d2py00849a |
This journal is © The Royal Society of Chemistry 2022 |