- Open Access
Lignin from hydrothermally pretreated grass biomass retards enzymatic cellulose degradation by acting as a physical barrier rather than by inducing nonproductive adsorption of enzymes
© The Author(s) 2018
- Received: 3 February 2018
- Accepted: 17 March 2018
- Published: 2 April 2018
Lignin is known to hinder efficient enzymatic conversion of lignocellulose in biorefining processes. In particular, nonproductive adsorption of cellulases onto lignin is considered a key mechanism to explain how lignin retards enzymatic cellulose conversion in extended reactions.
Lignin-rich residues (LRRs) were prepared via extensive enzymatic cellulose degradation of corn stover (Zea mays subsp. mays L.), Miscanthus × giganteus stalks (MS) and wheat straw (Triticum aestivum L.) (WS) samples that each had been hydrothermally pretreated at three severity factors (log R0) of 3.65, 3.83 and 3.97. The LRRs had different residual carbohydrate levels—the highest in MS; the lowest in WS. The residual carbohydrate was not traceable at the surface of the LRRs particles by ATR-FTIR analysis. The chemical properties of the lignin in the LRRs varied across the three types of biomass, but monolignols composition was not affected by the severity factor. When pure cellulose was added to a mixture of LRRs and a commercial cellulolytic enzyme preparation, the rate and extent of glucose release were unaffected by the presence of LRRs regardless of biomass type and severity factor, despite adsorption of the enzymes to the LRRs. Since the surface of the LRRs particles were covered by lignin, the data suggest that the retardation of enzymatic cellulose degradation during extended reaction on lignocellulosic substrates is due to physical blockage of the access of enzymes to the cellulose caused by the gradual accumulation of lignin at the surface of the biomass particles rather than by nonproductive enzyme adsorption.
The study suggests that lignin from hydrothermally pretreated grass biomass retards enzymatic cellulose degradation by acting as a physical barrier blocking the access of enzymes to cellulose rather than by inducing retardation through nonproductive adsorption of enzymes.
- Enzymatic hydrolysis
- S/G ratio
- β-O-4 linkage
- Apparent surface abundance
- Physical barrier
Optimal utilization of lignocellulosic biomass is vital for sustainable production of food, feed, fuels, chemicals, and materials. Hydrothermal pretreatment (HTP) and other types of physicochemical pretreatment methods are used to overcome the recalcitrance of the lignocellulosic biomass feedstocks to allow efficient enzymatic and biological processing [1, 2]. HTP of lignocellulosic biomass is known to remove parts of the hemicellulose fraction, thereby resulting in a cellulose-enriched fiber fraction which is more amenable to cellulase-catalyzed saccharification; depending on the pretreatment severity .
On the other hand, the presence of lignin in hydrothermally pretreated lignocellulosic biomass has also been considered as an important limiting factor in the enzymatic hydrolysis of cellulose [4, 5]. Lignin has thus been reported to promote nonproductive adsorption of the enzymes through charged and noncharged interactions and it may also act as a physical barrier that blocks the access of cellulolytic enzymes to cellulose [6–8]. Notably, nonproductive adsorption of cellulases to lignin has been considered as a key factor that limits the enzymatic conversion of pretreated biomass [4, 6, 9].
Available studies [10–18] have consistently shown that the enzymes are bound to isolated lignin materials from various biomasses and consequently the enzymes’ activity and/or the rate and extent of saccharification of model cellulose substrate in the presence of the isolated lignin were reduced. Observation of the latter has contributed to the use of the term “inhibitory effect” of lignin to enzymatic hydrolysis of cellulose in scientific literature.
Investigating the role of lignin as a physical barrier, however, can be difficult and complicated. Primarily this is due to modification of the lignin structure [19, 20] and its redistribution in the cell wall matrix [21, 22] after hydrothermal or dilute acid pretreatment. Advanced microscopy and imaging techniques have been developed to visualize components of lignocellulosic biomass, although extracting quantitative information can sometimes be difficult .
Recently, we have published a systematic study where industrially relevant Poaceae biomass feedstocks, namely corn stover, Miscanthus × giganteus stalks and wheat straw were hydrothermally pretreated at different severity levels. Via utilizing several quantitative and semiquantitative approaches, we proposed that surface properties, including apparent surface abundance of lignin as semiquantitatively determined by attenuated total reflectance Fourier transform infrared (ATR-FTIR) spectroscopy were correlated to the digestibility of biomass .
The objective of the present study was to further elucidate the role of lignin in retarding enzymatic cellulose degradation. This was done by simultaneously studying both enzyme–lignin interaction and the physicochemical properties and apparent surface abundance of lignocellulose components. The experimental approach was performed in three steps. Firstly, lignin-rich residues (LRRs) from the abovementioned biomass feedstocks were isolated through extensive enzymatic hydrolysis and characterized comprehensively. The ensuing profile of the LRRs is expected to resemble the actual bioprocess residues from lignocellulosic ethanol/biorefinery plants and the procedure is also expected to only exert minimal changes to the lignin structure. Secondly, the LRRs were assessed for their effect on the activity of state-of-the-art commercial cellulolytic enzyme mixture using relevant dosage. Thirdly, the data obtained in previous steps were extrapolated to explain what seemed to have occurred during actual extended enzymatic biomass hydrolysis reaction.
Composition of lignin-rich residues
Composition of pretreated biomass feedstocks and their resulting isolated lignin-rich residues
Biomass—log R 0
Pretreated biomass feedstocks
(% w/w DM)
55.5 ± 3.1ab
14.7 ± 0.8a
23.8 ± 2.3cd
20.9 ± 0.5b
5.4 ± 0.2a
60.4 ± 1.3f
55.7 ± 1.3ab
11.2 ± 0.5b
22.4 ± 0.8d
14.5 ± 0.1d
3.2 ± 0.1bc
75.4 ± 0.9de
61.2 ± 1.1a
6.4 ± 0.1e
19.9 ± 3.9d
7.2 ± 0.2f
1.6 ± 0.0e
79.5 ± 1.6bc
53.6 ± 2.6b
11.3 ± 0.4b
32.5 ± 2.1ab
33.9 ± 0.7a
5.7 ± 0.1a
58.5 ± 0.7f
54.7 ± 2.8ab
7.8 ± 0.6d
32.2 ± 0.5ab
18.9 ± 0.6c
3.0 ± 0.1c
73.1 ± 0.8e
55.9 ± 2.1ab
4.5 ± 0.2f
35.6 ± 0.3a
11.7 ± 0.5e
1.4 ± 0.0e
81.9 ± 0.3b
54.8 ± 0.6ab
14.7 ± 0.0a
29.3 ± 0.7bc
13.7 ± 0.6d
3.4 ± 0.1b
77.7 ± 0.7cd
58.2 ± 4.7ab
9.8 ± 0.4c
30.8 ± 0.7ab
7.9 ± 0.0f
2.0 ± 0.0d
86.2 ± 0.1a
61.2 ± 2.5a
6.5 ± 0.2e
30.3 ± 1.1b
5.3 ± 0.1g
1.1 ± 0.0f
87.8 ± 1.0a
In order to investigate the accessibility of the residual carbohydrates, further enzymatic hydrolysis was done on the LRRs. The results showed that only negligible amounts of monosaccharides were released (Additional file 1: Table S1). This indicated that the remaining cellulose and hemicellulose fractions were not accessible to the enzymes; most likely due to the surface coverage by lignin. Therefore it can be assumed that adsorption of the enzymes onto residual cellulose is negligible.
In order to assess the apparent surface abundance of lignocellulose components in the LRRs, ATR-FTIR spectroscopy was utilized as described previously . However, when using the semiquantitative approach, the peak area values of the carbohydrates in the lignin-rich residues (LRRs) were too low for reasonable quantification. Upon examination of the ATR-FTIR spectra (Additional file 1: Figures S1–S3), apparently this was due to the diminishing intensity of carbohydrate peaks corresponding to cellulose (895 cm−1) and hemicellulose (1732 cm−1) after extensive enzymatic hydrolysis process. On the other hand, the peaks corresponding to lignin (835, 1419, 1432, 1508 and 1601 cm−1) increased greatly after hydrolysis. Since ATR-FTIR wavenumbers have limited depth of penetration (Table 3), these observations confirmed the previous observations and inference (Additional file 1: Table S1) that the carbohydrates in the lignin-rich residues were not present in the surface, conceivably due to being engulfed by lignin. A likely scenario therefore was that as cellulose hydrolysis progressed, the work of the enzymes was halted due to the increasing presence of lignin in the surface of the biomass particles which acted as physical barrier. However, since lignin has been reported to promote retardation through nonproductive adsorption, the interaction between lignin and LRRs should also be investigated.
Interaction between enzymes and lignin-rich residues
Several studies on the adsorption of cellulases on lignin materials isolated from various biomasses have found that adsorption of cellulases (or their adsorption parameters modeled with Langmuir isotherms) increase slightly with elevated severity factor [15, 25, 26], although one study found the opposite . In one study on lignin isolated from corn stover that had been hydrothermally pretreated at different severities, it was found that there were only minor differences in the binding capacity of cellulases, with only 6% of increase with severity factor (log R0) of 3.6–3.9 . These results imply that the applied severity factor during pretreatment does not always warrant a significant increase in adsorption of cellulolytic enzymes. However, separate tests need to be conducted to assess whether adsorption of enzymes has direct impact on their performance.
In Experiment I, despite the adsorption of enzymes from the commercial cellulolytic enzyme mixture on LRRs (Fig. 1), there was no reduction of enzymatic activity in saccharifying cellulose (Fig. 2a–c). Since the final enzyme dosage in the hydrolysis reaction was low (10 mg protein/g DM cellulose) and on par with that being used in large-scale process , it is less likely that the absence of any retardation of the glucose release was due to the excess of unbound enzymes. Furthermore, in Experiment II, the activity of unbound enzymes after adsorption was studied in a scenario as if the binding of the enzymes on lignin were irreversible by performing solid–liquid separation. The results showed that the activity of unbound enzymes alone (with reductions of 19–57% for the different LRRs across all time points) was not enough to degrade the added Avicel to the same rate and extent as that accomplished by the free enzymes that were not adsorbed on LRRs (Fig. 2d–f). This absence of retardation in Experiment I therefore indicated that the LRR-adsorbed cellulose degrading enzymes in the mixture were still active on the added cellulose despite the adsorption. The phenomenon has been shown previously where the enzymes adsorbed on insoluble lignin-rich solids obtained after hydrolysis of dilute acid pretreated corn stover can be recycled by adding fresh substrate to the residue . The finding thus led to two possibilities.
One possibility is that the enzymes were still active despite being bound on lignin [30, 31], likely since the binding occurred without impeding the active site of the enzymes. However, if this was the sole case, a pronounced decrease in cellulose hydrolysis should still be observed since adsorbed or immobilized cellulases were reported to have decreased activity [31, 32]. In contrary, Experiment I showed negligible effect of the presence of LRRs on enzymatic cellulose hydrolysis (Fig. 2a–c). Experiment I has been designed to expand the assessment of enzyme–lignin interaction. On the one hand, the preadsorption of the enzymes on lignin provided more difficulty for the enzymes to degrade the cellulose. On the other hand, the latter introduction of cellulose allowed the enzymes to display whether the binding on lignin is reversible. Therefore, by showing negligible difference in the Avicel hydrolysis (Fig. 2a–c), the results gave strong indication on the reversible binding nature of the enzymes on lignin, i.e. the more likely was the possibility that the adsorbed enzymes desorbed from the LRRs and then re-adsorbed onto Avicel and catalyzed the degradation. This is also supported by the previous findings that cellulases have higher affinity to cellulose or lignocellulosic biomass compared to lignin [16, 33]. The adsorption and desorption kinetics of individual monocomponent cellulases on lignin hence deserve further investigation in order to corroborate this hypothesis.
It is also important to note that the trend of the effect of LRRs on the enzymes was consistent throughout the tested grass biomass (Fig. 2a–c). In a previous study, LRR from hydrothermally pretreated spruce was found to reduce the rate and extent of Avicel hydrolysis by cellulases after incubation at 45 °C . In this work, there was no reduction discernible as a result of the presence of LRRs during reaction at 50 °C (Fig. 2a–c). The difference between the data in this study and the previously reported data on spruce is likely due to botanical origin of the lignin material. Hence this present work, along with other studies using LRRs from hydrothermally pretreated grasses, showed that the LRRs did not reduce the rate and extent of enzymatic cellulose hydrolysis despite some degree of enzyme adsorption on the LRRs [26, 34, 35].
Experiment II nevertheless validated that a portion of the commercial cellulolytic enzyme mixture did get adsorbed onto LRRs and thus was not recovered when the supernatant was transferred, thereby reducing the extent of Avicel hydrolysis (Fig. 2d–f). Since glucose release was compromised in Experiment II, it is plausible that the fraction of the adsorbed enzyme consisted of β-glucosidases (BGLs). Accordingly, BGL was reported previously to have the highest affinity toward lignin from steam-pretreated corn stover compared to other components of Cellic® CTec2 . However, the difference in the reduction of Avicel hydrolysis in Experiment II may be a result of the different affinities of other various enzyme components in the mixture to the different LRRs, as there was no distinct pattern in the overall protein adsorption (Fig. 1). Since the LRRs did not exert nonproductive adsorption and reduction of activity that distinguished them from one another, it can be expected that there were only minor changes in the chemical composition of the lignin.
Physical and chemical characterization of the lignin-rich residues
13C-1H HSQC contour integration values for inter-unit linkages in the lignin polymer of the lignin-rich residues
The reduction of ether β-O-4 linkages intensity is expected to occur as a result of increasing pretreatment severity as it is the most susceptible linkage to break during thermochemical treatment [19, 37–39]. However, the cleavage of β-O-4 was not significant with only 4–13% signal reduction in the contour integration values across biomass and severity levels (Table 2). In another study, an increase of HTP severity factor (log R0) from 2.76 (160 °C for 10 min) to 3.65 (190 °C for 10 min) resulted in a 700% drop of the relative abundance of β-O-4 linkages in wheat straw lignin . The minimal change in β-O-4 cleavage observed in this study therefore can be attributed to the narrower range of the HTP severity factor (log R0) being used (from 3.65 to 3.97). Stable contour integration values of covalent C–C bonds have also been reported across elevated severity either due to increase of temperature or addition of acid . Overall, the 2D NMR results suggested that the lignin in the LRRs did not undergo significant chemical changes within the tested severity factors.
ATR-FTIR assignments of wavenumbers used to measure peak area
Estimated penetration deptha (μm)
C–H out-of-plane in all position of H and in positions 2 and 6 of S units 
Anomeric C-groups, C1-H deformation, ring valence vibration (cellulose, wood, holocellulose) 
Aromatic skeletal vibrations combined with C–H in-plane deformation 
Other studies assessing biomass resulting from hydrothermal or dilute acid pretreated biomass have found that increasing pretreatment severity results in higher release of S units compared to G units in GS type lignin, thus reducing the S/G ratio [19, 45, 46]. However, it has also been reported that the S/G ratio is unaffected by pretreatment severity level [44, 47]. Apparently, the botanical origin of lignin as well as pretreatment method affect the S/G ratio. Since cleavage of β-O-4 linkages in the LRRs was minimum across the applied severity levels in this study (Table 2), it is conceivable that the S/G ratio did not change as β-O-4 linkage constitutes a significant fraction of linkages with syringyl units . Even though the monolignols content, especially the S/G ratio of lignin, may be related to biomass recalcitrance, the exact contribution is not clearly defined as conflicting trends across different feedstocks and pretreatment methods have been reported .
In this work, the results from Experiment II showed that the LRRs from CS had higher S/G ratio compared to the others (Figs. 3b and 4) and also gave less reduction of Avicel hydrolysis compared to LRRs from MS and WS (Fig. 2d–f). Accordingly, another study on isolated lignins from hardwood found that there were less adsorption on substrate with higher S/G ratio . However, this was not apparent from the adsorption experiment since the binding of total protein on LRRs from CS was not significantly lower than others (Fig. 1). Regardless, relative monolignols contents (Figs. 3 and 4) indicated that the chemical composition of the lignin did not change significantly across the tested hydrothermal pretreatment severity levels.
During HTP, the cleavage of inter-unit linkages such as β-O-4 bonds can occur, which will result in depolymerization of lignin polymer and subsequent decrease of Mw. On the other hand, at increased severity, condensation reactions can also occur due to the formation of new covalent bonds (C–C) which will result in lignin repolymerization and subsequent increase of Mw. Both reactions can occur competitively or either one can dominate [37, 39, 49–51], most likely subject to the botanical origin of the lignin as well as employed pretreatment method and severity factors. The GPC results therefore suggested that there were significantly more depolymerization reaction in the LRRs of WS across severity factors compared to that of CS and MS (Fig. 5).
Based on the 2D NMR results, depolymerization should be likely to have occurred although not to a great extent due to only minor reduction of β-O-4 linkage across the tested severity levels in the LRRs (Table 2). The slight increase in the β-5 bond of LRRs from MS (Table 2) can give indication of repolymerization reactions although it can be difficult to confirm. In any case, it is possible that competing repolymerization reactions might have occurred in the lignin polymers of LRRs from CS and MS which resulted in relatively stable distribution of molecular weight fractions across the severity levels. Alternatively, it has been known that guaiacyl (G) units tend to start condensation reaction more easily than the syringyl (S) units during thermochemical pretreatment and therefore are harder to remove [19, 45, 48, 49, 51]. Based on Py-GC–MS and ATR-FTIR, LRRs of MS and WS had lower S/G ratio than that of CS (Figs. 3b and 4); meaning that they had more G units. However, GPC results showed differently in which lignin depolymerization occurred to a greater extent in the LRRs of WS than others (Fig. 5).
This work showed that when viewing the LRRs as an exaggerated version of extensive cellulose hydrolysis, the residual carbohydrates contents were highest in the LRRs of MS (Table 1). The low extent of hydrolysis of MS correlated to our previous finding, where using ATR-FTIR, we previously showed that MS had the highest initial relative abundance of lignin in the surface prior to pretreatment (Fig. 6) . Following HTP, the apparent surface abundance of lignin in the biomass prior to enzymatic treatment increased with increasing severity factor although it was consistently lower in WS compared to CS and MS for each corresponding severity (Fig. 6) . Extrapolation of the insight from our previous finding to the present study suggests that as extensive cellulose hydrolysis progressed, the advance was retarded earlier in CS and MS which had higher apparent surface abundance of lignin than WS. This lower apparent surface abundance of lignin in pretreated WS (Fig. 6) corresponded to a greater extent of depolymerization of lignin in the LRRs of WS (Fig. 5). In contrast, the lignin in pretreated CS and MS with higher apparent surface abundance (Fig. 6) corresponded to lesser extent of lignin depolymerization (Fig. 5); indicating the possibility that lignin properties can affect its subsequent distribution. Therefore, it can be suggested that the lignin in pretreated CS and MS has become a more potent physical barrier that shielded the carbohydrates after pretreatment than the lignin in pretreated WS. This proposition is supported by the fact that the remaining carbohydrates in the LRRs (Table 1) were not accessible for release by enzymes (Additional file 1: Table S1) and that ATR-FTIR revealed increased presence of lignin in the surface but almost negligible carbohydrates (Additional file 1: Figures S1–S3). All in all, this study along with our previous work  and recent works by other groups [53–55] have emphasized the role of lignin as a physical barrier which hinders the accessibility of enzymes to the cellulose in lignocellulosic biomass during extended enzymatic treatment.
The study showed that enzymes from a commercial cellulolytic mixture adsorbed onto lignin-rich residues (LRRs) isolated from hydrothermally pretreated grass biomass. Although the adsorption reduced the free activity in the supernatant, the performance of the enzymes was not affected by the presence of LRRs. The applied pretreatment severity levels did not significantly affect lignin’s chemical composition, and while there were differences across biomass feedstocks, the differences had no impact on the adsorption of enzymes and their ability to saccharify cellulose. On the other hand, even though there was a positive correlation between the lignin content of the LRRs with severity level and biomass digestibility, the residual carbohydrates were not accessible due to physical obstruction by lignin. We suggest that the lignin surface coverage, plausibly due to its inherent physicochemical and structural properties, determines the degree of retardation of enzymatic cellulose degradation in lignocellulosic biomass feedstocks. Therefore, the role of lignin in impeding enzymatic degradation of cellulose can be defined more as a physical barrier which obstructs the access of enzymes to cellulose rather than acting as an “inhibitor” that promotes the loss of activity through nonproductive adsorption. This points to the need to better understand pretreatment and hydrolysis of biomass particles at the physical level where among others, the migration of lignin can be monitored both within micro- and ultrastructural scales of the plant cell wall. Based on the results obtained in the present study, it is also important to investigate the dynamics of nonproductive binding of cellulases and its monocomponent enzymes on lignin in order to assess if the adsorption of individual enzymes differs with various substrates.
Corn stover (Zea mays subsp. mays L.) (CS), Miscanthus × giganteus stalks (MS), and wheat straw (Triticum aestivum L.) (WS) were each hydrothermally pretreated at three severity factors (log R0): 3.65 (190 °C, 10 min), 3.83 (190 °C, 15 min), and 3.97 (195 °C, 15 min) as described previously . Composition of biomass fiber fraction was determined using strong acid hydrolysis procedure based on the protocol of the National Renewable Energy Laboratory (NREL) .
Isolation of lignin-rich residues (LRRs)
Isolation of the LRRs was performed according to Rahikainen et al.  with modifications. Extensive cellulose hydrolysis of the biomass was performed using Cellic® CTec3 (Novozymes, Bagsværd, Denmark) with a dosage of 60 mg protein/g DM biomass in 0.05 M sodium citrate buffer pH 5.0 at 50 °C with 7.5% DM solids loading for 72 h. After every 24 h of hydrolysis, the whole suspension was centrifuged, and then, fresh amount of buffer and enzyme were added as in the original amount. After 72 h, the suspension was sieved using 500-μm mesh and washed thrice using ultrapure water pH 2.50 acidified with HCl, freeze-dried, and then protease treated. The protease treatment of the residue was done using commercial protease from Bacillus licheniformis (Sigma-Aldrich, St. Louis, MO, USA) at 37 °C for 24 h at 5% DM solids loading and enzyme loading of 20 mg protein/g DM residue) in 0.5 M NaHCO3/Na2CO3 buffer pH 9.60. After protease treatment, the LRRs were freeze-dried, ground, and used for analyses and experiments. Composition of the LRRs was determined using strong acid hydrolysis procedure . Elemental analysis was performed on the LRRs to confirm the removal of adsorbed proteins using an EA3000 element analyzer with acetanilide as standard (Euro Vector Instruments & Software, Milan, Italy). After protease treatment, the nitrogen content was significantly reduced, indicating that the remaining adsorbed enzymes after extensive hydrolysis had been removed (Additional file 1: Table S3).
Adsorption experiment was performed using Cellic® CTec3 (Novozymes A/S, Bagsværd, Denmark) with protein loading of 20 mg/g DM. The experiments were performed in triplicates at 1% DM lignin-rich residues in 0.05 M sodium citrate buffer pH 5.0 in 2 ml Protein LoBind® tubes (Eppendorf AG, Hamburg, Germany). The tubes were agitated using a tube revolver (Thermo Fisher Scientific Inc., Waltham, MA, USA) for 2 h at 15 RPM and incubated at 50 °C. After the experiments, liquid fractions were separated by centrifugation and stored frozen prior to analysis. The protein concentration in the liquid fraction was analyzed using ninhydrin method with bovine serum albumin (BSA) as standard [57, 58].
Effect of lignin-rich residues (LRRs) on the hydrolysis of cellulose
The effect of the isolated LRRs on the enzymatic hydrolysis of cellulose was assessed in two experiments. In Experiment I, 1 ml of 0.2 mg protein/ml Cellic® CTec3 (Novozymes A/S, Bagsværd, Denmark) was incubated with 1% DM LRRs as in the previous adsorption experiment study for 2 h at 50 °C. Then 0.5 ml suspension of 6% DM Avicel PH-101 (Sigma-Aldrich, St. Louis, MO, USA) was added into the mixture which resulted in final total solids concentration of 2.67% DM. The final enzyme dosage being used in Experiment I therefore was 6.7 mg protein/g DM total solids (LRR and Avicel) or equivalent to 10 mg protein/g DM cellulose (Avicel). As a control, the same amount of enzyme was incubated without LRRs. In Experiment II, 1 ml of 0.2 mg protein/ml Cellic® CTec3 (Novozymes A/S, Bagsværd, Denmark) was also incubated with 1% DM LRRs as in the previous adsorption experiment study for 2 h at 50 °C. The suspension was then centrifuged, and 0.75 ml of the supernatant was mixed with 0.375 ml of 6% DM Avicel PH-101 (Sigma-Aldrich, St. Louis, MO, USA) suspension which resulted in final solids concentration of 2% DM. As a control, the same amount of liquid was taken from the same amount of enzyme that was incubated without the LRRs. In both experiments, the hydrolysis of added Avicel was performed in ThermoMixer Comfort (Eppendorf AG, Hamburg, Germany) at 50 °C and agitation of 1250 RPM with samples being taken after 1, 6 and 24 h. Samples for each time points were boiled for 10 min, centrifuged, and the supernatant was analyzed for glucose using Dionex ICS-5000 system (DionexCorp, Sunnyvale, CA, USA) as explained previously . Both experiments were performed in duplicate and enzyme and substrate blanks were used for correction.
Pyrolysis-gas chromatography–mass spectrometry (Py-GC–MS)
The lignin-rich residues were pyrolyzed in duplicates according to Jensen et al.  with modifications. The samples were prepared by transferring about 100–200 µg to a pyrolysis tube. Pyrolysis was performed under a He flow of 100 ml/min at 500 °C (calibrated as sample received temperature). The pyrolysis temperature was held for 20 s by the PYRO pyrolysis unit (GERSTEL, Mülheim an der Ruhr, Germany). The transfer line was held at 320 °C and pyrolysates were carried onto the chromatographic column with a 100:1 split in the inlet held at 300 °C. The pyrolysates were separated and detected using 7890B GC and 5977A MSD series GC–MS (Agilent, St. Clara, CA, USA) equipped with an VF-5 ms (60 m, 0.25 mm, 0.25 µm) (Agilent, St. Clara, CA, USA) column. All compounds used for calculating monolignol ratios were identified by standards or published mass spectra . The compounds were grouped according to methoxylation into H, G or S (Additional file 1: Table S4). Monolignol ratios were calculated as the peak area of the specific monolignol in proportion to the total peak area of the three monolignols.
Gel permeation chromatography (GPC)
The molecular weight (Mw) distribution of aromatic compounds in the LRR samples was determined by gel permeation chromatography (GPC) using a procedure adapted from a previous study . Separation of compounds was performed on a PolarSil column (300 × 8 mm, 5 µm, 100 Å) (PSS Polymer Standards Service, Mainz, Germany) at 70 °C in a 9:1 (v/v) dimethyl sulfoxide/water eluent with 0.05 M LiBr. The LRR samples were dissolved in the eluent at concentrations of 2 g/l with sonication and overnight mixing. Detection was performed using UV–Vis detector at 280 nm. Tannic acid (1701 Da), β-O-4 dimer (320 Da) and vanillin (152 Da) were used as standards to approximate the molecular weight distribution in the chromatograms.
The lignin-rich residues were prepared in DMSO-d6/pyridine-d5 for whole plant cell wall characterization and were analyzed through heteronuclear single quantum coherence (HSQC) experiments according to the established protocol  as reported previously .
Attenuated total reflectance-Fourier transform infrared (ATR-FTIR) spectroscopy
ATR-FTIR measurements were performed on the lignin-rich residues with five technical replicates using a Nicolet 6700 FT-IR, Pike Technologies GladiATR diamond spectrometer (Thermo Scientific, Waltham, MA, USA) as described previously . The IR spectra (Additional file 1: Figures S1–S3) were normalized using Standard Normal Variate . The peaks included are listed in Table 3. Monolignols ratios of syringyl (S), guaiacyl (G) and p-hydroxyphenyl (H) units of lignin, namely H/G and S/G ratios, were assessed by calculating the ratio of estimated peak areas of 835/1508 and 1601/1508 cm−1 respectively.
One-way analysis of variance (ANOVA) was performed using JMP 13 (SAS Institute Inc., Cary, NC, USA) with post hoc analysis using Tukey–Kramer’s Honestly Significant Difference (HSD) test at P ≤ 0.05. Connecting letters were used to report the significant statistical difference among the mean values where different letters indicate that the compared mean values are significantly different. For example, values with the letters “A,” “B,” and “C” are significantly different from one another, whereas those with the letter “A” are not significantly different.
DTD, MP, HJ, and AM planned the study, analyzed the results, and wrote the manuscript. DTD performed experiments, analyzed data, and drafted the manuscript. MMJ and MG performed Py-GC–MS and GPC and participated in the corresponding data analysis. MO participated in the preparation and compositional analysis of the lignin-rich residues and adsorption experiment. AJ acquired 2D NMR spectra and participated in NMR data analysis. LGT directed the ATR-FTIR data acquisition and participated in the analysis of the spectra. All the authors read and approved the final manuscript.
The Combustion and Harmful Emission Control research center is thanked for providing access to elemental analyzer. René Thrane is thanked for assistance in freeze-drying.
The authors declare that they have no competing interest.
Availability of data and materials
All data generated and analyzed during this study are included in the manuscript and its additional file in form of graphs and tables.
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All authors agree to the submission.
Ethics approval and consent to participate
This study was funded by the BioValue SPIR, Strategic Platform for Innovation and Research on value added products from biomass, which is co-funded by The Innovation Fund Denmark, Case No: 0603-00522B.
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