Ronny
Wahlström
*,
Stella
Rovio
and
Anna
Suurnäkki
VTT Technical Research Center of Finland, P.O. Box 1000, FI-02044 VTT, Espoo, Finland. E-mail: ronny.wahlstrom@vtt.fi; Fax: +358 20 722 7071; Tel: +358 40 02 54 073
First published on 10th April 2012
The enzymatic hydrolysis of cellulose in ionic liquid (IL) containing systems has recently received a lot of interest as a pretreatment in biomass conversion to liquid biofuels and chemicals. In this paper we present a study in which the activity and action of two Trichoderma reesei endoglucanases, Cel7B and Cel5A, were evaluated in aqueous solutions containing 0–90% (v/v) of the ionic liquids 1,3-dimethylimidazolium dimethylphosphate or 1-ethyl-3-methylimidazolium acetate, using microcrystalline cellulose (Avicell) as a model substrate. The degree of hydrolysis was analysed by capillary electrophoresis of the hydrolysates and gel permeation chromatography of the remaining cellulose residues. Both of the employed ionic liquids severely inactivated the T. reesei endoglucanases. Only traces of soluble oligosaccharides were present in hydrolysis mixtures containing 40% (v/v) or more of ionic liquids. The employed ILs were found to have a basic impact on the hydrolysis environment, but it could be concluded that the basicity of the ILs was not the only reason for the cellulase inactivation. The effect of an IL on the cellulose binding module in Cel5A was evaluated by comparing the hydrolysis yields of the intact Cel5A and the Cel5A core lacking the cellulose binding module. In this study the cellulose binding module was found to be the most ionic liquid sensitive part of the enzymes used. Comparative data from the partial hydrolysis of an ionic liquid regenerated cellulose is also reported.
Natural cellulose is a semicrystalline polymer consisting of crystalline and amorphous regions.1 It is very recalcitrant towards enzymatic hydrolysis due to its high degree of crystallinity, low surface area for enzyme binding,6 and its general insolubility.2 In lignocellulosics, the presence of other biomass components further shelter the cellulose from hydrolysis.6 A great variety of chemical, physical and biological pretreatment methods have been proposed for lignocellulosic biomass for use prior to enzymatic total or partial hydrolysis.6,7 Typical to all of them is a high consumption of energy and often undesirable by-product formation,8 facts that render them economically and/or environmentally unfeasible for total hydrolysis.
During the last decade a growing interest in the dissolution of cellulose in ionic liquids (ILs), followed by subsequent homogeneous modification, or regeneration by the addition of a counter-solvent, has arisen. ILs are defined as salts with melting points below 100 °C.9 These compounds possess some very interesting solvent properties due to their dual ionic and organic nature. ILs have generally been considered as green solvents, mainly due to their thermal stability and negligible vapour pressure, which eliminates any VOC (volatile organic compound) emissions.10 As early as 1934 Graenacher received a patent on dissolving and processing cellulose in benzylpyridinium chloride.11 However, modifying cellulose in ionic liquids started receiving interest only after Swatloski et al. reported the dissolution of cellulose in 1-n-butyl-3-methylimidazolium chloride [BMIM]Cl in 2002.12 It has also been shown that even wood, in the form of saw dust or wood chips, can dissolve in some ionic liquids.13
Cellulases are the main enzymes for the enzymatic hydrolysis of cellulose. These enzymes have been studied in cellulose hydrolysis both as complex mixtures and in the monocomponent form. Cellulases may be divided into three types of functionalities, which work together synergistically: endoglucanases, which randomly hydrolyse the cellulose chain in its amorphous regions producing cellooligomers, exoglucanases, which hydrolyse the cellulose chains from either the reducing or the non-reducing end producing mainly cellobiose and β-glucosidases, which cleave the resulting cellobiose units produced by the glucanases.14
One of the earliest studies on the enzymatic hydrolysis of cellulose in aqueous ILs was published by Turner et al. in 2003.15 This study clearly demonstrated that ILs greatly inactivate cellulase enzymes. Dadi et al. showed that the enzymatic hydrolysis of cellulose might be greatly enhanced by IL pretreatments of the substrates.16 In this process concept, the enzymatic hydrolysis takes place in a separate process step after the regeneration of cellulose from the IL solution. The increase in reaction rates was attributed to the lower degree of crystallinity in the regenerated cellulose (RC). Kamiya et al. introduced the term “in situ saccharification”, where the regeneration of cellulose and the subsequent enzymatic hydrolysis are carried out in a one-pot procedure.17 The presence of 1,3-dimethylimidazolium diethylphosphate was reported to inactivate the cellulases, with very little enzymatic activity in IL contents over 40% (v/v). Several studies elucidating cellulase inactivation in ILs have been published since, employing different hydrolysis conditions, enzyme cocktails, ILs and substrates.8,18–27
Various factors affecting cellulase inactivation in ionic liquids have been proposed. Basic anions such as Cl−, Br−, NO3− and CF3SO3− in ILs seem to be strongly inactivating as they interfere with the hydrogen bond network keeping the enzyme together.28 Fluorinated anions, such as the BF4− and PF6−, have, on the other hand, been shown to be more compatible with enzymes in some cases. The “enzyme-friendliness” of ILs has been defined in terms of their chao- and chosmotropicity, as well as by using the Hofmeister series for predicting the effects of anions on enzymatic stability.29 The high viscosity of IL solutions also play a significant role in slowing down enzymatic reactions8,28 due to mass transfer constraints. It also remains unclear whether an enzyme is irreversibly denatured or simply inhibited by the presence of ILs.
In this paper we report how the presence of two hydrophilic, cellulose dissolving room-temperature ionic liquids, 1,3-dimethylimidazolium dimethylphosphate [DMIM]DMP and 1-ethyl-3-methylimidazolium acetate [EMIM]AcO affects the partial hydrolysis of microcrystalline cellulose (MCC) by two purified Trichoderma reesei endoglucanases, Cel7B (EGI) and Cel5A (EGII). These two ILs were chosen for this work because they are both hydrophilic, dissolve cellulose, and have been pointed out to be enzyme compatible to a certain degree.24,30 [DMIM]DMP is one of the most studied ILs in enzymatic hydrolysis. It has been found to be a strong candidate for use in biorefinery applications, as it combines good biomass dissolving capability with a certain degree of “enzyme-friendliness”.24 A major advantage is the fact that [DMIM]DMP may be produced on an industrial scale in a one-pot procedure without considerable by-product formation.31 [EMIM]AcO is known as a powerful cellulose solvent, but the enzyme compatibility of this IL has not been clarified conclusively. The enzymatic hydrolysis of MCC was carried out in the presence of 0–90% (v/v) of IL. After hydrolysis, the solid cellulose residue was analysed by gel-permeation chromatography (GPC) for changes in the molecular weight, and the soluble cellooligosaccharides were analysed using capillary electrophoresis (CE) with pre-column derivatization. Based on the results, the two ILs are compared both in terms of their interactions with the substrate and their effect on enzymatic activity.
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Fig. 1 Light microscopy pictures of microcrystalline cellulose suspended/dissolved in pure buffer (upper left), or 60 (upper right), 85 (lower left) or 90% (v/v) (lower right) [EMIM]AcO solutions in buffer. The magnification is 100. |
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Fig. 2 Light transmission (T) for aqueous cellulose suspensions/solutions in [DMIM]DMP and [EMIM]AcO at 45 °C. |
IR spectroscopy was used to determine the crystallinity of MCC after interactions with the different amounts of ILs in MCC–IL–buffer samples. The lateral order index (LOI), also known as the crystallinity index CrI,43 was calculated as the peak ratio α1437/α899.40 The LOI of commercial MCC was measured to be 1.1. As expected, the LOI of the regenerated cellulose (RC) was significantly lower with a value of 0.41–0.45. Surprisingly, the crystallinity of MCC that had been treated in 90% (v/v) [EMIM]AcO was even lower with values in the range 0.1–0.25. This difference in LOI values might be due to differences in the dissolution and regeneration conditions in preparing RC in pure [EMIM]AcO vs. the treatment of MCC during the hydrolyses. The LOI values of samples that had been treated in 90% (v/v) [DMIM]DMP were in the range 0.7–0.9, confirming that [DMIM]DMP is not capable of dissolving the MCC to a high extent nor in any other way to significantly alter the MCC structure under these conditions. Also the total crystallinity index (TCI) was calculated as the peak ratio α1378/α2900,41 but the TCI values did not correlate with the LOI values or the expected changes in crystallinity. Recently, similar conclusions about the LOI and TCI values for regenerated cellulosic materials were published by Zhao et al.26
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Fig. 3 Apparent pH values for ionic liquid in buffer solutions (pH 5.0). |
To find out whether the pH drift is one of the major reasons for the previously reported enzyme inactivation,8,15,17 a hydrolysis experiment at pH 7 in buffer was carried out and the saccharide yield and composition was analysed by CE. The hydrolysis yield of soluble oligosaccharides at pH 7 was 50% and 20% for Cel5A and Cel7B, respectively, as compared to the respective yields in buffer at pH 5 (Table 1 and 2). The oligosaccharide distribution was to some extent altered by the change in pH, as measured after 72 h of hydrolysis. The oligosaccharides formed were glucose, cellobiose and cellotriose; no larger oligosaccharides were found with CE. At pH 7 the Cel7B produced traces of cellotetraose and cellopentaose (results not shown), as well as cellotriose, which is not a normal product pattern of Cel7B under optimum conditions45 (Table 1). This would indicate a slowdown of the hydrolysis, yielding intermediary products, due to the deviation from the optimum pH. The fairly well retained hydrolytic activity of Cel5A at pH 7 (Table 2) is expected as this enzyme is known to be active (on β-glucan) over a wide pH window from at least pH 3 to pH 9.45 Cel7B was clearly more sensitive to the deviations from its optimum pH.
Cel7B | Formed soluble oligosaccharides/yield | |||||||
---|---|---|---|---|---|---|---|---|
2 h | 72 h | |||||||
Sample | Glc (mg L−1) | CB (mg L−1) | CTr (mg L−1) | Yield (%) | Glc (mg L−1) | CB (mg L−1) | CTr (mg L−1) | Yield (%) |
MCC, buffer (pH 5) | 29.7 | 112.3 | < LOD | 1.3 | 160.5 | 429.5 | 11.7 | 5.6 |
MCC, buffer (pH 7) | 7.9 | 41.7 | 13.1 | 0.6 | 14.9 | 79.0 | 24.2 | 1.1 |
MCC, 20% IL1 | 2.2 | 20.1 | < LOD | 0.2 | 19.0 | 90.8 | 3.6 | 1.0 |
MCC, 40% IL1 | < LOD | < LOD | < LOD | 0.0 | < LOD | 6.5 | < LOD | < 0.1 |
MCC, 20% IL2 | < LOD | 4.6 | 5.5 | < 0.1 | Traces | 4.4 | 6.5 | < 0.1 |
MCC, 40% IL2 | < LOD | < LOD | < LOD | 0.0 | < LOD | < LOD | < LOD | 0.0 |
RC, buffer (pH 5) | ND | ND | ND | ND | 425.8 | 799.8 | < LOD | 11.4 |
Cel5A | Formed soluble oligosaccharides/yield | |||||||
---|---|---|---|---|---|---|---|---|
2 h | 72 h | |||||||
Sample | Glc (mg L−1) | CB (mg L−1) | CTr (mg L−1) | Yield (%) | Glc (mg L−1) | CB (mg L−1) | CTr (mg L−1) | Yield (%) |
Buffer (pH 5) | 25.8 | 86.6 | 87.1 | 1.9 | 256.2 | 458.9 | 219.4 | 8.8 |
Buffer (pH 7) | 10.3 | 47.7 | 52.9 | 1.1 | 41.7 | 192.4 | 199.9 | 4.2 |
20% IL1 | 2.0 | 17.2 | < LOD | 0.3 | 25.4 | 94.1 | 89.4 | 2.0 |
40% IL1 | Traces | Traces | < LOD | 0.0 | < LOD | 3.3 | 4.8 | 0.1 |
90% IL1 | < LOD | < LOD | < LOD | 0.0 | < LOD | < LOD | < LOD | 0.0 |
20% IL2 | < LOD | 5.9 | 9.4 | 0.1 | Traces | 19.5 | 21.9 | 0.4 |
40% IL2 | < LOD | < LOD | < LOD | 0.0 | < LOD | < LOD | < LOD | 0.0 |
Cel5A Core, buffer pH 5 | ND | ND | ND | ND | 13.5 | 45.6 | 40.5 | 0.9 |
Cel5A Core, 20% IL1 | ND | ND | ND | ND | 8.3 | 48.1 | 47.9 | 1.0 |
Cel5A Core, 90% IL1 | ND | ND | ND | ND | < LOD | < LOD | < LOD | 0.0 |
RC, buffer (pH 5) | ND | ND | ND | ND | 572.2 | 865.6 | 392.3 | 17.1 |
According to the pH curves displayed in Fig. 3, a pH-value of 7.0 corresponds to roughly 60% (v/v) [DMIM]DMP or 40% (v/v) [EMIM]AcO in sodium citrate buffer. For neither Cel7B nor Cel5A no soluble oligosaccharides could be detected after 72 h of hydrolysis in the hydrolysis mixtures containing these amounts of [DMIM]DMP (results not shown) or [EMIM]AcO (Table 1 and 2). This clearly indicates, in the case of Cel5A, that the basic pH drift caused by the ILs is not the only reason for the enzyme's inactivation. Enzymatic activity decreases much faster with increasing IL content than the increase of pH gives reason to. This is also in line with the results of Engels et al.,8 where the pH was adjusted in the IL solutions, yet enzyme inactivation was observed in the presence of ILs. In the case of Cel7B, a major decrease is recorded both at pH 7 as well as when ILs are present allowing no conclusion to be made as to whether the reason for the drop is the changed pH or other effects caused by the presence of ILs.
Enzyme inactivation for Cel5A was studied with prolonged incubation times of 2 h and 72 h in 90% (v/v) [DMIM]DMP in hydrolysis conditions. Interestingly, the measured residual endoglucanase activity was at approximately the same level as that measured after 15 min incubation. This would indicate a very fast decrease in enzymatic activity when the enzyme is mixed with the IL, with an equilibrium settling after which the enzyme activity stays rather stable. It was further noticed that 10 min boiling inactivated the enzyme in 90% (v/v) [DMIM]DMP solution hardly at all. These results were verified to be due to the enzymatic activity by varying the amount of enzyme in the measurements, as well as the incubation time in the residual activity measurement.
To explore the function of the CBM in the presence of ILs, hydrolysis of MCC was carried out in a buffer at pH 5 (optimum conditions) and in 20 and 90% (v/v) of [DMIM]DMP with both intact Cel5A containing CBM and Cel5A without CBM (Cel5A Core) (Table 2). The cellulose hydrolysis yield at optimum conditions with the Cel5A Core was considerably lower than that with the intact Cel5A, resulting in about 10% of the yield of the intact enzyme. Interestingly, the hydrolysis yield of the Cel5A Core was the same in 20% (v/v) of [DMIM]DMP as in the optimum conditions. The product distribution was, however, somewhat different with lower amounts of glucose and higher amounts of cellobiose and cellotriose after the IL containing hydrolysis as compared to that after the hydrolysis in pure buffer. The hydrolysis activity of the intact enzyme decreased, however, drastically in the presence of 20% (v/v) of [DMIM]DMP as compared with its activity in the buffer. According to these results, the action of CBM of Cel5A seems to be highly affected by the presence of [DMIM]DMP. The effect of this IL on the structure of the CBM and its substrate recognition ability, both potential factors affecting the CBM action on the cellulose, needs to be elucidated in further studies. In the high [DMIM]DMP concentration of 90% (v/v) no oligosaccharides could be detected in the hydrolysate for neither Cel5A nor Cel5A Core.
Both [DMIM]DMP and [EMIM]AcO are very inactivating for the studied endoglucanases, [EMIM]AcO even more so than [DMIM]DMP. More cellobiose and cellotriose and less glucose was produced in the presence of both [DMIM]DMP and [EMIM]AcO as compared to the product distribution in the citrate buffer reference at pH 5 (Table 1 and 2). This suggests an overall slowing down of the hydrolysis. The total yield of solubilized saccharides was significantly decreased as the IL concentration increased. With only 20% (v/v) of [DMIM]DMP present in the hydrolysis mixture, the overall yield decreased to approximately 20% of the reference in 72 h of hydrolysis. 40% (v/v) of this IL only allowed very low hydrolysis rates for both the enzymes. In 20% (v/v) [EMIM]AcO extremely low concentrations of oligosaccharides were detected as compared to the amounts found in 20% (v/v) [DMIM]DMP. In 40% (v/v) of [EMIM]AcO neither of the studied enzymes were able to catalyse the formation of any oligosaccharides. Cel5A, being more active for MCC in the reference buffer system, also seemed to be slightly more tolerant towards the ILs, and especially against [EMIM]AcO, than Cel7B. In hydrolysis samples containing an IL in the range 60–90% (v/v) of IL no soluble oligosaccharides could be detected after enzymatic treatment.
The kinetics of oligosaccharide formation in MCC hydrolysis was different for the two enzymes when [EMIM]AcO was present. Cel7B produced a low amount of cellobiose and cellotriose during the first two hours and was then totally inactivated with no further saccharide formation (Table 1). Cel5A was still able to increase the amount of solubilized saccharides in these circumstances after a two hour hydrolysis (Table 2). In [DMIM]DMP this same difference between the enzymes was not observed, but both enzymes were able to produce saccharides during the course of the 72 h MCC hydrolysis also after the 2 h time point. It could be concluded that the inactivating effect of the ILs was different for the two T. reesei endoglucanases studied and that the inactivation is dependent on both the enzyme and the IL it is exposed to.
Sample | Time (h) | Mn (g mol−1) | Mw (g mol−1) | StDev(Mw) | Polydispersity |
---|---|---|---|---|---|
MCC | |||||
Reference (MCC, untreated) | 10![]() |
50![]() |
5500 | 5.16 | |
Cel7B, buffer pH 5 | 72 | 12![]() |
49![]() |
1600 | 4.02 |
Cel5A, buffer pH5 | 72 | 11![]() |
48![]() |
5000 | 4.33 |
Cel5A Core, buffer pH5 | 72 | 9000 | 49![]() |
3000 | 5.29 |
Cel7B, buffer pH 7 | 72 | 11![]() |
50![]() |
400 | 4.36 |
Cel5A, buffer pH 7 | 72 | 10![]() |
47![]() |
4300 | 4.89 |
Reference, buffer | 72 | 10![]() |
47![]() |
3800 | 4.62 |
Cel7B, 90% [DMIM]DMP | 2 | 10![]() |
45![]() |
4900 | 4.50 |
Cel7B, 90% [DMIM]DMP | 24 | 7000 | 34![]() |
400 | 4.84 |
Cel7B, 90% [DMIM]DMP | 72 | 8000 | 36![]() |
3200 | 4.66 |
Cel5A, 90% [DMIM]DMP | 2 | 9000 | 41![]() |
1000 | 4.57 |
Cel5A, 90% [DMIM]DMP | 24 | 7000 | 36![]() |
6000 | 4.95 |
Cel5A, 90% [DMIM]DMP | 72 | 9000 | 35![]() |
1600 | 4.10 |
Reference, 90% [DMIM]DMP | 2 | 10![]() |
48![]() |
4400 | 4.68 |
Reference, 90% [DMIM]DMP | 24 | 8000 | 45![]() |
3600 | 5.68 |
Reference, 90% [DMIM]DMP | 72 | 11![]() |
49![]() |
3500 | 4.56 |
Cel5A Core 90% [DMIM]DMP | 2 | 9000 | 43![]() |
600 | 4.57 |
Cel5A Core 90% [DMIM]DMP | 72 | 9000 | 40![]() |
1800 | 4.33 |
Cel7B double enzyme dosage, 90% [DMIM]DMP | 72 | 8000 | 40![]() |
3700 | 4.75 |
Cel5A double enzyme dosage, 90% [DMIM]DMP | 72 | 8000 | 34![]() |
2100 | 4.50 |
RC | |||||
RC (untreated) | 9000 | 47![]() |
4200 | 5.15 | |
RC, Cel7B, buffer pH 5 | 72 | 7000 | 32![]() |
800 | 4.78 |
RC, Cel5A, buffer pH 5 | 72 | 5000 | 12![]() |
500 | 2.45 |
RC reference, buffer | 72 | 9000 | 44![]() |
600 | 4.91 |
A decrease of 20–30% in the weight average molecular weight (Mw), as well as decreases in the number average molecular weight (Mn) for samples treated enzymatically in 90% (v/v) [DMIM]DMP, could be observed (Table 3). The changes in the molecular weight distribution can clearly be seen when comparing the distributions of the samples (Fig. 4). The decrease in Mw was observed for both Cel7B and Cel5A. Cel5A Core was also able to reduce the Mw, even if not to the same extent as the two intact endoglucanases. This effect was noticed to increase with increasing hydrolysis time. The Mw was not affected either by the presence of BSA or by addition of endoglucanase, which had been inactivated by boiling. It is possible that the 90% (v/v) [DMIM]DMP solution has sufficient dissolving power to alter the MCC structure during hydrolysis to a more accessible substrate for the enzyme, the conditions in this solution at the same time being such that the enzyme still retains some of its cellulose chain scission activity. The decrease in the molecular weight of cellulose was not observed in any other conditions than in the 90% (v/v) [DMIM]DMP solutions. It was shown by the residual activity measurements in 90% (v/v) [DMIM]DMP, that both Cel7B and Cel5A retain about 50% of their activity at least for 15 min in this media.
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Fig. 4 Molecular weight distributions for MCC samples after 72 h enzymatic treatments in 90% (v/v) [DMIM]DMP. |
Interestingly, the decrease in Mw for MCC noticed in 90% (v/v) [DMIM]DMP was not accompanied by any detectable formation of soluble cellooligomers. This may imply that the enzymes' activity is altered by the conditions applied or that the enzymes are able to carry out random chain scission on the substrate which is in a new, easier accessible form due to the interactions with the IL. Hydrolysis experiments were also carried out with a doubled enzyme dosage (Table 3). Increasing the enzyme dosage did not lead to an increased rate of cellulose chain scission. According to this result, the limiting factor is not the IL induced enzyme inactivation, but must rather be substrate dependent. The possibility that the cellulose could be enzymatically hydrolysed during its regeneration after the hydrolysis cannot be ruled out, especially as we have shown that 10 min boiling does not completely inactivate the enzymes. Further studies are needed to fully clarify the mode of action of T. reesei endoglucanases in the MCC in the presence of high concentrations of [DMIM]DMP.
In [EMIM]AcO, no decrease in Mw was noticed for any concentration of this IL in the hydrolysis mixture (results not shown). Although [EMIM]AcO is a much more powerful cellulose solvent than [DMIM]DMP, it is probable that this IL totally inactivates the studied endoglucanases, in contrast to [DMIM]DMP.
The RC was very efficiently hydrolysed by both Cel7B and Cel5A under optimum conditions at pH 5, both in terms of the produced cellooligomers (Table 1 and 2) and in terms of the decreased Mw (Table 3). The difference between the two endoglucanases was large: Cel7B was able to cause a decrease in Mw of 27% against the reference, whereas Cel5A caused a decrease in Mw of 73%, which is also clearly seen by comparing the molecular weight distributions (Fig. 5). This change in Mw was accompanied by a roughly doubled production of soluble oligosaccharides in the hydrolysate (Table 1 and 2).
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Fig. 5 Molecular weight distributions for cellulose regenerated in ionic liquid (RC) samples after 72 h enzymatic treatment in buffer at pH 5. |
Soluble oligosaccharides were not produced in the enzymatic hydrolysis at IL concentrations of more than 40% (v/v). Surprisingly, both the studied endoglucanases appeared, however, to reduce the molecular weight of the solid cellulose residue in hydrolysis mixtures containing 90% (v/v) [DMIM]DMP. Similar phenomena were not observed in systems containing [EMIM]AcO nor in any other attempted conditions including the optimum conditions in buffer at pH 5. Further studies are needed to fully clarify the mode of action of T. reesei endoglucanases in the MCC in the presence of high concentrations of [DMIM]DMP and during the regeneration of the cellulose sample. IL pretreated, regenerated cellulose was shown to yield by far the best hydrolysis results both in terms of solubilized oligosaccharides and the decreased molecular weight of the cellulose residue.
Both [DMIM]DMP and [EMIM]AcO were found to cause a strong basic drift to the hydrolysis mixtures' pH values, but it could be established that the pH drift was not the main cause for the low observed enzymatic activities in the presence of these ILs. The IL containing matrices were also found to be challenging for the analytics. In particular, the DNS assay and HPLC techniques were disturbed when attempting to analyse samples with high IL concentrations. The cellooligomers could be quantified in the presence of ILs employing CE techniques with pre-column derivatization.
There is a great need to further develop IL compatible analytical methods, if accurate research results are to be obtained in this research field. There is also a clear need for new, more enzyme-friendly ILs, which combine properties such as low price, recyclability, non-toxicity and of course the ability to dissolve biomass. Stabilizing the cellulase enzymes in these systems as well as finding cost effective methods to separate the hydrolysis products from the IL containing hydrolysates are future challenges.
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