M. A.
Johns
ab,
A.
Bernardes
c,
E. Ribeiro
De Azevêdo
c,
F. E. G.
Guimarães
c,
J. P.
Lowe
d,
E. M.
Gale‡
ad,
I.
Polikarpov
c,
J. L.
Scott
*ad and
R. I.
Sharma
*ab
aCentre for Sustainable Chemical Technologies, University of Bath, BA2 7AY, UK. E-mail: j.l.scott@bath.ac.uk; r.sharma@bath.ac.uk
bDepartment of Chemical Engineering, University of Bath, BA2 7AY, UK
cSão Carlos Institute of Physics, University of São Paulo, 13566-590, Brazil
dDepartment of Chemistry, University of Bath, BA2 7AY, UK
First published on 3rd May 2017
Cellulose-based hydrogel materials prepared by regeneration from cellulose solutions in ionic liquids, or ionic liquid containing solvent mixtures (organic electrolyte solutions), are becoming widely used in a range of applications from tissue scaffolds to membrane ionic diodes. In all such applications knowledge of the nature of the hydrogel with regards to porosity (pore size and tortuosity) and material structure and surface properties (crystallinity and hydrophobicity) is critical. Here we report significant changes in hydrogel properties, based on the choice of cellulose raw material (α- or bacterial cellulose – with differing degree of polymerization) and regeneration solvent (methanol or water). Focus is on bioaffinity applications, but the findings have wide ramifications, including in biomedical applications and cellulose saccharification. Specifically, we report that the choice of cellulose and regeneration solvent influences the surface area accessible to a family 1 carbohydrate-binding module (CBM), CBM affinity for the cellulose material, and rate of migration through the hydrogel. By regenerating bacterial cellulose in water, a maximum accessible surface area of 33 m2 g−1 was achieved. However, the highest CBM migration rate, 1.76 μm2 min−1, was attained by regenerating α-cellulose in methanol, which also resulted in the maximum affinity of the biomolecule for the material. Thus, it is clear that if regenerated cellulose hydrogels are to be used as support materials in bioaffinity (or other) applications, a balance between accessible surface area and affinity, or migration rate, must be achieved.
Carbohydrate-binding modules (CBMs) are protein domains found in cellulose-degrading enzymes that are responsible for guiding the appended catalytic domain of the enzyme to the cellulose surface.12 They can be independently expressed via recombinant plasmid cloning,13 enabling their use in bioaffinity attachment without modification, or grafting, of the cellulose substrate. Bioaffinity attachment is of particular interest as it ensures controlled orientation of the active molecule, resulting in improved activity, and is generally reversible despite the attached agent being strongly bound.14 This enables the production of novel biocatalysts and biosorbents with enhanced performance;15–18 support matrices for affinity chromatography and biosensors;19–21 and biocompatible scaffolds for human tissue growth.22–24
Tomme et al. previously reported that CBMs belonging to family 1, such as CBM1 of cellobiohydrolase I from Trichoderma harzianum (ThCBMCBHI), used in this work, reversibly bind to cellulose.25 This provides the opportunity to develop separation and purification applications, or regenerable biosensors, both of which require reversible binding of the active biomolecule.14 In order to assess whether cellulose hydrogels regenerated from ionic liquids are suitable supports for these applications, and to develop an understanding of their subsequent degradation rate, three parameters need to be investigated: (i) the accessible surface area of the hydrogel; (ii) the CBM partition constant; and (iii) the CBM diffusion rate.
It is desirable that the accessible surface area of the hydrogel is high, as this minimizes the mass of cellulose required for the application. It might also be expected to enable a higher rate of hydrolysis. In the same vein, a high CBM partition constant (a measurement that describes the affinity of the CBM for the material) is desirable in order to minimise excess CBM remaining in solution once the CBM has adsorbed onto the material. This is more important than the accessible surface area for bioaffinity applications given that cellulose is inexpensive compared to biomolecules, which require laborious expression, isolation and purification. Finally, a high CBM diffusion rate is desirable, as this will minimize the time required to load the hydrogel with the CBM and aid its subsequent removal. This is of importance at an industrial scale, as time is directly linked to cost.
It is known that family 1 CBMs preferentially bind to surfaces that are crystalline and hydrophobic.12,26,27 Therefore, we investigated hydrogels regenerated from an ionic liquid/co-solvent mixture (organic electrolyte solution) comprised of 30:70 1-ethyl-3-methyl imidazolium acetate:dimethyl sulfoxide ([EMIm][OAc]:DMSO) by weight using either methanol, or water, as the anti-solvent. Such materials are designated regenerated in methanol (rM), or regenerated in water (rW), respectively. The effect of the cellulose degree of polymerization (DP) on the resulting pore structure was evaluated using α-cellulose (AC), DP: 500–1300,28 and bacterial cellulose (BC), DP: 2000–6000.29 Herein, we demonstrate that the crystallinity, hydrophobicity and tortuosity of the regenerated hydrogel is dependent on both the type of cellulose and the anti-solvent used to regenerate the hydrogel, which, in turn affects the affinity of the CBM for the material and also modulates the rate of CBM migration within the hydrogel.
Transformed E. coli cells were cultured in LB broth containing kanamycin (50 μg mL−1) and chloramphenicol (34 μg mL−1) at 37 °C. After the medium absorbance at 600 nm reached 0.8, protein expression was induced with 1 mM isopropyl-β-D-thiogalactopyranoside and cells incubated for 16 h at 18 °C. The cells were harvested by centrifugation and resuspended in buffer A (20 mM Tris pH 7.5, 300 mM NaCl, 5% glycerol, 1 mM phenylmethanesulfonylfluoride and 4.3 M 2-mercaptoethanol). The sample was sonicated to disrupt the cells and centrifuged at 14000 rpm for 40 min. The soluble fraction of ThCBM1CBHI + SUMO was submitted to Ni2+ affinity purification. Buffer A was used to wash the set proteins/resin and protein elution was achieved with an imidazole gradient through a gradual increase of buffer B (20 mM Tris pH 7.5, 150 mM NaCl, 300 mM imidazole, 5% glycerol, and 4.3 M 2-mercaptoethanol). All the eluted samples were analyzed by 15% (wt/wt) SDS-PAGE.
The melting point depression, ΔT, is related to the pore radius, r, via the bulk properties of the probe liquid, P, as described by the Gibbs–Thomson equation:
Besides the averaged T2 values, the measurement of the decay of the CPMG echo train, CPMG decay SCPMG(t), T2 distribution profiles, g(T2), associated with distribution of pore sizes and variations in the water mobility within the pores, can be obtained using a non-negative least square procedure also known as a numerical inverse Laplace transform (ILT) to fit the SCPMG(t) curves.39,40 In this case, an ILT method implemented in Matlab was used.
Carbohydrate-binding module (CBM) depletion isotherms were constructed by incubating a 78.5 mm2 piece of the produced cellulose hydrogels with various concentrations (6.25–200 μM) of ThCBMCBHI in 100 μL of 50 mM PBS pH 7.0. Controls without cellulose were included and all experiments were conducted in triplicate. Samples were incubated at 4 °C for 24 h with agitation (roller table); 2 μL of the supernatant were removed and the concentration of free protein calculated by the absorbance measured at 280 nm using a NanoDrop 2000 Spectrophotometer (Thermos Fisher Scientific). The concentration of the bound ThCBMCBHI was calculated from the difference in initial and final ThCBMCBHI concentration in the supernatant.
Partition constants were obtained from the depletion isotherms (plot of final concentration versus mass of molecular probe adsorbed per gram of cellulose) after fitting of the raw data to a Langmuir-type adsorption model:
Rearrangement of the equation enabled calculation of Nm and K (Table S4, ESI†) for the molecular probes by plotting C/N versus C (Fig. S2 and S3, ESI†):
S = NmaNAv |
Cellulose hydrogel samples, 134.2 mm2, were incubated with fluorescein-modified ThCBMCBHI at a concentration of 10 nM for 19 h at 16 °C. The samples were then washed twice with PBS before being analysed using a Zeiss LSM 780 confocal microscope. Images were taken using a 405 nm diode laser at 17% power output, an excitation wavelength of 488 nm and absorption wavelength of 525 nm. An area of the sample was selectively bleached by multiple passes of the laser operating at 100% power until the fluorescence intensity of the area had halved (Fig. S5, ESI†). Images of the sample were then taken every minute for 1 h to measure recovery.
Theoretical fluorescence recovery curves based on the equation developed by Axelrod et al.41 were applied to the raw data in order to calculate the maximum fluorescence intensity recovery and the recovery half-life, i.e. the time required for the intensity of the bleached area to recover its intensity to half that of the final intensity value:
Sample | Density [kg m−3] | Porosity [%] | Crystallinity index | Modal nanopore diametera [nm] | Median micropore diameterb [nm] | Nano:micro pore ratioc |
---|---|---|---|---|---|---|
a Determined from NMR cryoporometry. b Determined from SEM micrographs. c Determined from NMR relaxometry studies. | ||||||
ACrM | 17 ± 1 | 99 | 0.18 | 50 | 226 | 10:1 |
ACrW | 22 ± 2 | 99 | 0.27 | 36 | 224 | 12:1 |
BCrM | 18 ± 1 | 99 | 0.19 | 54 | 190 | 5:1 |
BCrW | 17 ± 1 | 99 | 0.32 | 44 | 206 | 6:1 |
To probe the pore structure of the hydrogels without drying, two NMR techniques were employed: relaxometry and cryoporometry. In the former the dependence of proton transverse relaxation time (T2) and surface to volume ratio of pores was exploited. To complement this, and overcome difficulties in defining pore diameters,38 cryoporometry was used to probe specific pore size (<100 nm).46,47
The ILT of the CPMG decays obtained for the hydrogels revealed a T2 distribution profile with three distinct peaks. The peak at the highest T2 value is ascribed to the bulk water in the PBS, which is justified by the comparison with the T2 distribution profile obtained for the pure solution (Fig. 2C, inset).
The absence of a precise value for the relaxivity constant of water (PBS) inside cellulose pores frustrates association of T2 distributions with specific pore diameters. However, based on previously published data48 and on the averaged T2 values reported for pure water filling pores of known dimensions in cellulose,49–52 the relaxivity of pure water inside cellulose pores can be estimated to be in the range 10−6–10−7 nm s−1. Thus, using the relation between pore dimension T2 and relaxivity constant previously reported,48 the T2 range from 10–100 ms was ascribed to pores with dimensions in the range 10–100 nm and the T2 range from 100 ms to 1 s to pores with dimensions in the range 100 nm to a few μm. Thus, in Fig. 2C, the peaks at the shorter T2 values reflect nanopores, while the peaks with intermediate T2 reflect micropores. The peak corresponding to nanopores for AC reflected a smaller median pore diameter than that for BC, whilst hydrogels regenerated in methanol exhibited larger pores than those regenerated in water. NMR cryoporometry confirmed these observations, yielding a modal pore diameter of 36 nm for AC regenerated in water and 54 nm for BC regenerated in methanol (Fig. 2B and Table 1). It is of interest to note that Östlund et al. reported a pore radius distribution between 2–15 nm, based on NMR cryoporometry for cellulose samples regenerated from [EMIm][OAc] only,10 whilst the distribution in these hydrogels is between 10–70 nm, suggesting that the ratio of ionic liquid to co-solvent in the organic electrolyte solution used could influence the pore size of the resultant regenerated hydrogels, providing further opportunities to tune porosity.
NMR relaxometry studies revealed that micropores (above the range that can be probed with NMR cryoporometry) in AC exhibited a slightly larger median diameter than those in BC, as confirmed by analysis of SEM micrographs (Fig. 2A and Table 1). Significantly more nanopores were present in AC, as reflected in the ratio between the integrated nano- and micropore peak areas in the relaxometry data: that of AC was double that of BC (Table 1). In both cases, hydrogels regenerated in water show a 20% increase in nano- to micropore ratio versus those regenerated in methanol. To validate these results, and to discern whether such differences were important at a molecular scale, passive MB adsorption (used to characterize cotton fibers)53 was conducted. This enabled calculation of the cellulose surface area in the never-dried hydrogels, whilst providing a molecular probe small enough to access pores inaccessible to the larger CBM. (MB has an occupied surface area of 197.2 Å2 whilst ThCBMCBHI has a maximum occupied area of approximately 985 Å2, assuming a globular structure.54,55)
MB adsorption isotherms (Fig. 3a) revealed that BCrM had a lower surface area than ACrW (Table 2), in accordance with the observation that ACrW has a higher population of nanopores with smaller diameters (Table 1). The choice of cellulose influences the surface area by a factor of 1.6 (totalAC/totalBC), whilst the choice of anti-solvent affects the surface area by a factor of 1.2 (totalrW/totalrM).
Sample | MB specific surface area [m2 g−1] | MB partition constant [×10−3 L g−1] | MB partition constant [×10−3 L m−2] | CBM specific surface area [m2 g−1] | CBM partition constant [×10−3 L g−1] | CBM partition constant [×10−3 L m−2] |
---|---|---|---|---|---|---|
ACrM | 47 | 855 | 18.3 | 14 | 53 | 3.8 |
ACrW | 56 | 874 | 15.5 | 16 | 43 | 2.7 |
BCrM | 30 | 288 | 9.5 | 29 | 70 | 2.4 |
BCrW | 35 | 236 | 6.8 | 33 | 76 | 2.3 |
The surface area available for CBM attachment was also affected by the cellulose and anti-solvent type: rW hydrogels had a 1.2 increase in the ThCBMCBHI accessible surface area, due either to the higher proportion of nanopores with smaller diameters, or to the increase in crystallinity, compared to rM hydrogels. However, the use of AC resulted in a reduction of the surface area accessible to ThCBMCBHI by a factor of 0.4. It is hypothesised that a significant proportion of the pores in the AC samples accessible to MB are inaccessible to ThCBMCBHI (due to its larger size). Of the pore surface accessible to MB, 95% is accessible to ThCBMCBHI in hydrogels prepared from BC, whilst only 24% is accessible in hydrogels prepared from AC. This is supported by the nanopore:micropore ratios derived from the NMR relaxometry experiments (Table 1).
It is apparent that both the cellulose type (differing by DP only) and anti-solvent identity influenced the partition constants of MB (Table 2). MB partition constants measured for AC derived hydrogels are higher than for BC derived hydrogels and this may reflect differences in processing of the raw materials used.¶ CBM partition constants expressed in units of L m−2 (which more accurately reflects the surfaces available for adsorption of the probe molecules) gave distinctly larger values for rM samples versus rW samples when MB was used as the probe molecule. It has been reported that the partition constant for monosaccharide adsorption increased with the hydrophobicity index of the monosaccharide.56 Considering this to reflect in the reverse, i.e. adsorption onto polysaccharide surfaces, this might suggest greater hydrophobicity of surfaces in rM samples versus rW samples. This reflects previously published data pertaining to crystallinity: Östlund et al. argued that faster rates of demixing in water ‘trap’ the methylhydroxyl groups in the gauche–trans formation that is found in cellulose II.10 This results in a higher crystallinity for samples regenerated in water than those regenerated in methanol, where the methylhydroxyl groups adopt the more energetically favourable gauche–gauche confirmation, demonstrated computationally by Liu et al.57 If samples regenerated in methanol are more hydrophobic – due either to the conformation of the methylhydroxyl groups, or to the specific crystalline faces exposed – this would account for the observed difference. No such differences are noted in binding of ThCBMCBHI, with partition constants ranging between 3.8 and 2.3 mL m−2, reflecting the inaccessibility of the smaller pores to the large biomolecule (Table 2).
It is also of note that the partition constants expressed per unit mass, reported here for a family 1 CBM, are two orders of magnitude lower than those reported previously: a partition constant of 1.0 × 105 M−1 was reported for T. reesei CBMCBHI on native BC,25 and 4.9 L g−1 on microcrystalline cellulose;58 compared to 1.5 × 103 M−1 and 7.6 × 10−2 L g−1 on BCrW in this work. This reflects the lower degree of crystallinity in these regenerated samples, although, as previously discussed in the literature, these values do not take into account the accessible surface area.59
To test the hypothesis that some pores are inaccessible to CBMs, the rates of diffusion of fluorescently tagged ThCBMCBHI in hydrogels were determined from rates of recovery of fluorescent intensity after bleaching, using confocal microscopy. Recovery of the fluorescence intensity after bleaching is observed (Fig. 4), confirming that ThCBMCBHI is reversibly bound to the cellulose, in agreement with previous reports.25 The differences in the recovery half-lives and subsequent diffusion coefficients of the samples can be attributed to three different effects: (i) the pore structure of the hydrogels – a structure with fewer pores accessible to the CBM is more tortuous, resulting in a lower CBM diffusion rate and thus a longer recovery period; (ii) the affinity of the CBM to the cellulose, a higher partition constant resulting in a higher diffusion rate; and (iii) the hydrophobicity of the sample – it has been reported, based on computational simulations, that CBM could diffuse from hydrophilic to hydrophobic surfaces, but that the reverse transition was not observed in 43 ms of simulation,27 suggesting that a slower diffusion rate would be observed along surfaces with more hydrophilic character.
Given that the diffusion coefficient increases by a factor of 1.5 for AC compared to BC (Table 3), it is apparent that the affinity of the CBM for the cellulose surfaces is more important than the hydrogel tortuosity (assumed to be proportional to the difference in accessible surface area for ThCBMCBHI compared to MB). With regards to the anti-solvent type, rM hydrogels increase the diffusion coefficient by a factor of 2.2 over rW hydrogels. In this instance, the tortuosity and presumed hydrophobicity of the hydrogel are more important than the CBM affinity.
Sample | I max | k [min−1] | τ D [min] | t 1/2 [min] | D [μm2 min−1] |
---|---|---|---|---|---|
ACrM | 0.91 | 2.00 | 6.3 | 7.8 | 1.76 |
ACrW | 0.86 | 2.01 | 15.3 | 21.6 | 0.73 |
BCrM | 0.90 | 2.00 | 10.4 | 13.2 | 1.07 |
BCrW | 0.96 | 2.01 | 20.3 | 22.5 | 0.55 |
Specifically, the choice of cellulose starting material (with different DP) and anti-solvent used in generating cellulose hydrogels from solutions containing ionic liquids influence the crystallinity and pore structure of the resulting hydrogel. In turn, these affect the tortuosity and hydrophobicity of the porous material and, thus, the affinity of molecules adsorbing onto and migrating through, the hydrogel. Small molecules, such as the widely used probe methylene blue, do not yield information that can be extrapolated to larger probes, such as proteins, including CBMs. It is also clear that compromises may need to be made between the maximum accessible surface area for the CBM, here 33 m2 g−1 for bacterial cellulose regenerated in water, and maximum CBM partition constant per unit area and CBM diffusion coefficient, here 3.8 mL m−2 and 1.76 μm2 min−1 for α-cellulose regenerated in methanol. Thus, cellulose hydrogels optimized for various CBM-based bioaffinity applications may be prepared by manipulating the cellulose DP and anti-solvent. For example, the use of methanol to regenerate the hydrogel will lead to a higher enzymatic hydrolysis rate due to the increased CBM migration rate. In addition, bacterial cellulose has been widely posited as a biocompatible material and many potential applications of such hydrogels will rely on hydrogel structure.
Footnotes |
† Electronic supplementary information (ESI) available: Methylene blue HPLC calibration curve, C versus C/N plots for methylene blue and ThCBM1CBHI adsorption isotherms, Nm and K values for methylene blue and ThCBM1CBHI adsorption isotherms, bleaching images demonstrating fluorescent recovery. See DOI: 10.1039/c7tb00176b |
‡ Current address: School of Experimental Psychology, University of Bristol, BS8 1TH, UK. |
§ While BC is often ascribed to production by a particular strain, it can be more productive to use mixed cultures, such as those used in production of the drink ‘kombucha’, followed by appropriate purification, particularly where the material is then dissolved so removing any structural features. Reva et al., have reported that the core of such communities are comprised of acetobacteria of two genera, Komagataeibacter (formerly Gluconacetobacter) and Gluconobacter.60 |
¶ AC materials may be subjected to an acid wash during purification potentially leading to introduction of a very small number of acid groups on the surfaces that would bind a positively charged probe, such as MB, strongly. |
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