Abstract
Pretreatment of miscanthus is essential for efficient enzymatic production of cellulosic ethanol. This study reports a possible pretreatment method for miscanthus using aqueous ethylenediamine (EDA) for 30 min at 180 °C with or without ammonia. The mass ratio of miscanthus to EDA was varied from 1:3, 1:1, and 1:0.5, keeping the mass ratio of miscanthus to liquid (EDA + Water) constant at 1:8. The ammonia-to-miscanthus ratio was 1:0.25. After pretreatment with a ratio of 1:3 miscanthus to EDA, about 75 % of the lignin was removed from the raw miscanthus with 90 % retention of cellulose and 50 % of hemicellulose in the recovered solid. Enzymatic hydrolysis of the recovered solid miscanthus gave 63 % glucose and 62 % xylose conversion after 72 h. EDA provides an effective pretreatment for miscanthus, achieving good delignification and enhanced sugar yield by enzyme hydrolysis. Results using aqueous EDA with or without ammonia are much better than those using hot water and compare favorably with those using aqueous ammonia. The delignification efficiency of EDA pretreatment is high compared to that for hot-water pretreatment and is nearly as efficient as that obtained for aqueous-ammonia pretreatment.
Similar content being viewed by others
Avoid common mistakes on your manuscript.
Introduction
Economic and environmental concerns about the continued use of fossil fuels have prompted a search for alternative fuels using sustainable lignocellulosic biomass feedstock (Carroll and Somerville 2009). Conversion of abundant and renewable lignocellulosic biomass to bioethanol as a transportation fuel provides a possible option to reduce greenhouse gas emissions and fossil fuel consumption (Jordan et al. 2012). Miscanthus is a suitable biomass feedstock because it has high carbohydrate density and low fertilizer requirements for growth (Padmanabhan et al. 2012; de Vrije et al. 2009; Carroll and Somerville 2009; Brosse et al. 2012).
The primary constituents of miscanthus biomass are cellulose, hemicellulose, and lignin (Brosse et al. 2010, 2012; de Vrije et al. 2009; Carroll and Somerville 2009). For efficient production of cellulosic biofuels, miscanthus must be pretreated to overcome the barriers that hinder the hydrolysis of cellulose and hemicellulose to fermentable sugars (Kumar et al. 2009; Rodriguez et al. 2011; Shill et al. 2011; Alvira et al. 2010; Agbor et al. 2011; Cao et al. 2012). To facilitate enzymatic hydrolysis, an effective pretreatment must remove a significant fraction of lignin and perhaps, reduce the crystallinity of cellulose (Kumar et al. 2009; Shill et al. 2011). By decreasing the adherence of lignin to cellulose, and by disrupting the cellulose crystal structure, the barriers to hydrolysis are reduced; hydrolytic enzymes can then access the carbohydrates more easily (Geng and Henderson 2012; Klein-Marcuschamer et al. 2010).
A wide variety of pretreatments has been studied leading to various degrees of success (Blanch et al. 2011; Sousa et al. 2009; Kim et al. 2011). Of these, organosolv pretreatment has long been employed for delignification (Brosse et al. 2009, 2010). Organic solvents, with a little amount of inorganic acid as catalyst, can achieve a good degree of delignification (El Hage et al. 2009). Various studies in the paper-and-pulp industries have suggested that a combination of alkali and an organic solvent can yield a cellulose-rich pulp with a low amount of lignin (Abbot and Bolker 1982; Cochaux et al. 1995). Taking some clues from these studies, several research groups have employed combination of ammonia or methyl amine with organic solvents or ionic liquids for delignification of biomass (Cho et al. 2008; Cochaux et al. 1995; Rodriguez and Jimenez 2008; Sarwar et al. 2001; Abbot and Bolker 1982). Also, our recent work on delignification of miscanthus using a combination of EDA with organic solvents or ionic liquids suggests that EDA helps to cleave the lignin-carbohydrate link leading to good removal of lignin (Padmanabhan et al. 2012). EDA provides an added advantage with respect to higher alkalinity (pH > 12), which is favorable for the removal of lignin from miscanthus.
Pretreatment is the most expensive step in the overall production of bioethanol fuel (Klein-Marcuschamer et al. 2010; Tao et al. 2011). Therefore, it is desirable to minimize the loading of reagents or solvents in biomass treatment while nevertheless achieving a high sugar yield. To determine the viability of EDA in the pretreatment of miscanthus, we examine the effects of low and high EDA loadings to miscanthus (0.5:1, 1:1, 3:1). In addition to reporting EDA-based-pretreatment results, this work also gives a brief comparison with two well-known pretreatment methods: auto-hydrolysis (hot water) or aqueous ammonia.
Materials and methods
Raw materials and feedstock
Miscanthus (Miscanthus × giganteus) samples, obtained from the University of Illinois at Urbana-Champaign, were milled to 4-mm particles using a rotary mill (Hetsch). These particles were air-dried and stored in a sealed container. The moisture content of the miscanthus was 6.1 % determined using a halogen-moisture analyzer (Mettler-Toledo). Table 1 shows the composition of the raw untreated Miscanthus × giganteus determined using the procedures recommended by the National Renewable Energy Laboratory (NREL) and other recent publications (Sluiter et al. 2010a, b; Templeton et al. 2010; Ibáñez and Bauer 2014).
EDA was purchased from Sigma-Aldrich (USA) with a purity of 99.5 % and used as received. Compressed anhydrous ammonia with a purity of 99.99 % was purchased from Praxair, USA.
Cellobiase enzyme from Aspergillus niger and Cellulase enzyme produced from Trichoderma reesei ATCC 26921 were obtained from Sigma-Aldrich (St. Louis, MO). All enzymes were stored at 4 °C until use for hydrolysis. Cellulase and cellobiase (β-glucosidase) activities were 700 and 250 U/g, as provided by the supplier.
Citrate buffer was made from anhydrous citric acid (Fisher Scientific) and sodium citrate dehydrate (Research Organics Inc). pH was measured using a Mettler-Toledo pH meter. Sodium azide, 0.5 % (w/v), was obtained from Ricca Chemical Company and used as received.
Pretreatment procedure
EDA pretreatment
Figure 1 shows a schematic pretreatment diagram. Miscanthus and EDA were placed inside a batch pressure reactor (Moline Parr Instruments) with a capacity of ca. 20 cm3. One gram of miscanthus was added to a variable amount of EDA to achieve the desired miscanthus-to-EDA ratio for a particular pretreatment. Deionized milli-Q water was subsequently added until the total net weight of the solid–solvents mixture was 8 g. If the pretreatment used gaseous ammonia, the mixture was pressurized with 10 bar ammonia.
The reactor was placed in a temperature-controlled oil bath at 180 °C for 30 min. The reactor was then removed from the bath and cooled to room temperature. If the reactor contained ammonia, the ammonia was flashed after cooling.
The slurry was filtered. The liquid phase (EDA, water and dissolved biomass) was collected using vacuum filtration and stored for composition analysis. The remaining solid phase (recovered solid) was washed with water until pH 7 was achieved.
For each pretreatment condition, the pretreatment was replicated five times. Chemical composition analysis was done in triplicate, and enzymatic hydrolysis was done in duplicate, all with good reproducibility.
Auto-hydrolysis
Auto-hydrolysis experiments were carried out in the batch reactors mentioned in the previous section. Miscanthus-to-water ratio was set to 1:8 (w/w) and the pretreatment was carried out for 30 min at 180 °C. After 30 min, the slurry was cooled to room temperature, filtered using Whatman 41 filter paper to separate the liquid from the solid. The solid was dried in an oven at 105 °C for 12 h. The liquid was stored for chemical composition analysis. The chemical composition analysis of the solid followed the NREL protocol summarized here and in our previous publications (Padmanabhan et al. 2011; Rodriguez et al. 2011; Sluiter et al. 2010a, b).
Aqueous Ammonia
1 g of 4-mm-particle miscanthus and 10 gm of 5 or 30 % aqueous ammonia were placed in the pressurized autoclave. After 30 min at 180 °C, the miscanthus + ammonia slurry was cooled to room temperature prior to solid–liquid separation by filtration.
Chemical composition analysis of untreated and pretreated solid miscanthus
Analysis of untreated and pretreated miscanthus followed the protocols mentioned in recent publication of Ibáñez and Bauer (2014). This method is essentially a modification of NREL protocol to accommodate smaller size samples (Sluiter et al. 2010a, b; Templeton et al. 2010). The details of the protocols can be found in the publication of Ibáñez and Bauer (2014). A brief summary of the method employed is summarized here. The original and the recovered solid were dried in an oven at 105 °C at atmospheric pressure overnight until its dry weight did not change. The mass of the solid was then measured using a Mettler-Toledo electronic weighing balance with a precision of ±0.0001 g.
To obtain a material balance, amounts of cellulose, hemicellulose, and lignin present in the recovered solid were determined based on products obtained from acid hydrolysis. Three 50-mg samples of the dried solid were placed in separate 17-mL glass autoclave tubes. Half a milliliter of 72 % H2SO4 aqueous solution was then added to each tube. The hydrolysis was allowed to proceed for 1 h at room temperature. Brief vortexing with a Fisher Scientific digital vortex mixer was done every 10 min during the reaction to improve solid–liquid contact. After 1 h, 14 mL of water were added to reduce the acid concentration to 4 wt%. The tubes were then autoclaved at 121 °C and 1.38 bar for 1 h. The contents of the tube were cooled prior to filtration using glass filters (Millipore, Ireland).
The liquid phase from acid hydrolysis contained sugars and minor amounts of degradation products, mainly furfural and 5-hydroxymethylfurfural (HMF), in addition to any acid-soluble lignin. The solid residue contained acid-insoluble lignin and ash.
A one-milliliter aliquot of the liquid filtrate was filtered again using a 200-nm filtering disc and then analyzed using a Shimazdu HPLC equipped with a 300-mm × 7.8 mm Aminex HPX-87H column (Bio-Rad Laboratories) and a refractive-index detector. The mobile phase was 0.001 N–H2SO4 aqueous solution at a flow rate of 0.6 mL/min. The injection volume was 20 μL. The concentrations of sugars and degradation products were determined using previously established calibration curves.
The cellulose content in the original or recovered miscanthus was calculated from the concentrations of glucose and HMF. The hemicellulose content was calculated from the concentrations of xylose, arabinose, acetate, and furfural. These calculations followed the standard NREL analytical procedure.
The acid-soluble-lignin content is determined by analyzing the ultraviolet absorbance of the liquid filtrate at 205 nm using an Agilent 8453 UV–Vis spectrophotometer. An aliquot of the filtrate was diluted as needed (such that the absorbance was in the range 0.3–0.7) and placed in quartz cuvettes. The percent acid-soluble lignin was calculated from
The acid-insoluble lignin is the difference between the dry weight of solid residue from acid hydrolysis and its weight after it was ashed. To calculate the dry weight, the solid residue after filtering the autoclaved contents was oven-dried at 105 °C overnight; this weight was recorded. The dried solid was then placed in aluminum pans of known mass. The pan is then placed in a furnace and ashed by raising the temperature to 575 °C for 3–4 h. The aluminum pans had previously been ashed using the same thermal treatment to avoid errors due to residual organic substances on the pan. The percent acid-insoluble lignin was calculated from
The total lignin content is the sum of the acid-soluble and acid-insoluble lignin.
Enzymatic hydrolysis
The washed recovered solid was placed in a 125 mL Erlenmeyer flask. For 1 g of recovered biomass, 50 mL of citrate buffer solution (50 mM, 4.8–5.0 pH), 4.00 mL sodium azide solution (0.5 % w/v), was added to the Erlenmeyer flask. The purpose of sodium azide is to inhibit any microbial growth during enzyme hydrolysis. Cellulase and β-glucosidase were added at a loading of 20 FPU (Filter Paper Unit) per gram of cellulose. Cellulase measurement units (FPU) were determined according to the procedure described by Ghose (1987). Enzymatic hydrolysis was conducted at 50 °C in an Innova 44-series incubator with shaking at 150 revolutions per minute. The pH of the system was maintained in the range of 4.8–5.0, which is considered as the optimal conditions for cellulase enzymes (Ghose 1987). Aliquots of 200 μL of supernatant were taken after 72 h. Each aliquot was diluted by a factor of two and analyzed using a Shimadzu HPLC.
Conversions of cellulose to glucose and hemicellulose to xylose are calculated using Eqs. 3 and 4. We report conversions for the pretreated solid miscanthus, excluding what dissolved in the aqueous phase.
In the above equation, the constant 0.9 accounts for hydration of cellulose to produce glucose.
In Eq. (4), the constant 0.88 accounts for hydration of hemicellulose to produce xylose.
Additional production of glucose and xylose (not studied here) can be obtained from cellulose and hemicellulose in aqueous EDA stream.
Results and discussion
Effect of EDA with and without ammonia on delignification of miscanthus
Delignification of miscanthus after pretreatment is calculated from:
Figure 2 and Tables 1 and 2 show the effect of EDA on delignification of miscanthus with and without ammonia. Compared to hot-water pretreated miscanthus, addition of EDA leads to significant lignin removal. As expected, increasing concentration of EDA leads to higher delignification. When the miscanthus-to-EDA mass ratio is 1:0.5, nearly 58 % delignification is achieved. Higher miscanthus-to-EDA ratio (1:3) raises lignin removal to approximately 72 %. Because EDA has appreciable hydrogen basicity, it provides delignification larger than those using conventional polar solvents (Ishikura 2011; Padmanabhan et al. 2012). Our previous work on solubility studies of miscanthus using COSMO-RS (conductor-like screening model–real solvents) indicated that ammonia, amines and EDA favor interactions with the phenolic-OH group of lignin due to their strong hydrogen-bond basicity (Rodriguez et al. 2011; Padmanabhan et al. 2011). This basicity contributes to better solubilization and removal of lignin.
Figure 2 also shows that delignification of miscanthus with EDA and ammonia is nearly the same as that of EDA without ammonia. About 75 % of lignin is removed upon addition of ammonia to 1:3 mass ratio of miscanthus to EDA. Because there is no significant improvement in delignification upon addition of ammonia, EDA alone appears to be sufficient for good lignin removal.
Comparison of EDA delignification with delignification using hot water or aqueous ammonia
Figure 2 shows the extent of delignification of miscanthus using: (a) auto-hydrolysis, (b) aqueous ammonia and (c) EDA (with and without ammonia). The extent of delignification for EDA pretreatment is nearly same as that using aqueous ammonia for pretreatment of miscanthus and other biomass feedstock (Kurakake et al. 2001; Wyman et al. 2009; Boonmanumsin et al. 2012; Kim et al. 2009). Delignification results obtained here are comparable to those reported elsewhere for alkaline pretreatment (Wang et al. 2004, 2012; Elander et al. 2009; Gupta and Lee 2010; Tao et al. 2011; Park et al. 2010). Our previously reported work on pretreatment of miscanthus using aqueous ammonia (10, 20 and 30 %) achieves nearly 75 % delignification (Liu et al. 2013).
Figure 2 shows that both aqueous ammonia and EDA provide similar delignification despite different chemical mechanisms. For aqueous ammonia, the OH− nucleophile is responsible for the breaking of lignin–carbohydrate interactions, whereas for EDA the interaction mostly follows from the two NH2 groups present in the diamine.
Figure 2 suggests that hot-water pretreatment alone is not sufficient to remove a significant amount of lignin. Only 10–12 % delignification was achieved with the hot-water pretreatment at 180º C, consistent with results reported by others (Ingram et al. 2011b; Wyman et al. 2011). Ingram et al., and Wormeyer et al., have compared lignin removal efficiency of hot water versus organosolv pretreatment for wheat straw feedstock (Wormeyer et al. 2011; Ingram et al. 2011a, b). Their studies confirm that organosolv pretreatment is more efficient than hot water for lignin removal.
Low and high loading of EDA gives delignification similar to that reported in our previous work on binary solvent mixtures of EDA with a polar organic solvent or an ionic liquid (Padmanabhan et al. 2012). Previous work, however, used higher loadings of EDA and a smaller miscanthus particle size (80 μm). In this study, with an eye toward economic process design, we have explored delignification using low-to-high loadings of EDA with larger miscanthus particle size (4 mm).
Delignification of miscanthus in aqueous EDA may be due to a reaction that decreases the molecular weight of lignin (Helmy and Aboustate 1993). Several alkaline pretreatment studies suggest that addition of alkali prevents repolymerization of lignin oligomers (Jahan and Farouqui 2000; Wang et al. 2010; Sarwar et al. 2001; Rodriguez and Jimenez 2008). Addition of ammonia or EDA to hot water leads to better solubilization of lignin in the liquid alkaline phase (Jahan and Farouqui 2002; Sun et al. 2010).
Enzymatic hydrolysis of EDA-pretreated miscanthus
Figure 3 shows results of enzymatic hydrolysis following three different pretreatments. For comparison, Fig. 3 also presents results for enzymatic hydrolysis of raw untreated miscanthus. As expected, untreated miscanthus shows very low conversion of carbohydrates to fermentable sugars, even after 1 week. Our studies show, once again, that pretreatment is necessary to break the recalcitrance of miscanthus for enzymatic hydrolysis to sugars.
Auto-hydrolysis pretreatment without alkali gives only minor conversion of cellulose to glucose after 72 h. The conversion is only about 20 %. This low conversion indicates that alkali is necessary to achieve the structural changes in cellulose required for significant delignification.
Pretreatment of miscanthus with EDA at various loadings with or without ammonia gives much better enzymatic hydrolysis compared to that for untreated or hot-water pretreated miscanthus. There is a strong correlation relating higher EDA loadings for improved conversion to glucose and xylose. A higher ratio of miscanthus to EDA corresponds to higher pH. As the EDA loading increases from 0.5:1 to 3:1(keeping temperature constant), enzymatic conversion improves from 27 to 63 % after 72 h.
The observed increase in conversion to sugars probably follows from higher delignification that enhances accessibility of enzymes to cellulose and hemicellulose. However, removal of lignin alone may not be sufficient for higher enzymatic conversions; probably, it is also important to bring changes in the structure of cellulose and to remove hemicellulose. Addition of ammonia to EDA does not appear to produce significant increase in sugar yield after enzyme hydrolysis.
The Tables 1 and 2 show that about one-half of the hemicellulose is retained in the recovered solid while the other half is dissolved in the liquid phase. Hemicellulose in the recovered solid may limit the accessibility of Cellulase enzymes. Hemicellulose oligomers provide a barrier to Cellulase enzymes, as shown by Wymann and coworkers (Qing and Wyman 2011; Kumar and Wyman 2009). Their results show that either addition of supplemental Xylanase enzymes or removal of hemicellulose raises the conversion of cellulose to glucose.
Although special hemicellulase enzymes were not added in our work, we nevertheless observed production of xylose. Some hemicellulase (xylanase) enzymes are present in the Celluclast enzyme cocktail even after purification, as indicated by the supplier. Similar to that of glucose, xylose yield rises upon increasing the loading of EDA. Upon raising EDA loading from 0.5:1 to 3:1, hemicellulose to xylose conversion increases from 33 to 55 % after 72 h. For auto-hydrolysis, hemicellulose to xylose conversion rate is same as that of cellulose to glucose. The presence of hemicellulose and lignin may perhaps be limiting the conversion rate. On the other hand, for ammonia alone treatment as well as for EDA with and without treatment, hemicellulose to xylose conversion rate raises with increase in the loadings of either ammonia or EDA. This perhaps confirms the observation that removal of hemicellulose as well as lignin may help achieve enzyme conversion.
Conclusion
EDA provides an effective pretreatment for miscanthus, leading to good lignin removal and enhanced sugar yield by enzyme hydrolysis. Up to 75 % of lignin is removed leading to a yield of 63 % glucose and 62 % xylose from the recovered solid. The delignification efficiency of EDA pretreatment is high compared to that for hot-water pretreatment and is nearly as efficient as that obtained for aqueous-ammonia pretreatment. Addition of ammonia to EDA does not increase enzymatic conversion to sugars despite more removal of lignin and hemicellulose. Increasing EDA loading provides improved conversion of cellulose to sugars. Chemical composition analysis shows that better lignin removal improves sugar yields. About one-half of hemicellulose is removed from the solid during pretreatment; it is dissolved in the liquid phase, where, following adjustments to lower pH, it can be converted to xylose.
Abbreviations
- EDA:
-
Ethylene diamine
- NREL:
-
National Renewable Energy Laboratory
- HMF:
-
5 hydroxymethyl furfural
- FPU:
-
Filter paper units
- HPLC:
-
High-pressure liquid chromatography
- COSMO-RS:
-
Conductor-like screening model–real solvents
References
Abbot J, Bolker HI (1982) How amines accelerate delignification. Tappi 65(2):37–40
Agbor VB, Cicek N, Sparling R, Berlin A, Levin DB (2011) Biomass pretreatment: fundamentals toward application. Biotechnol Adv 29(6):675–685. doi:10.1016/j.biotechadv.2011.05.005
Alvira P, Tomas-Pejo E, Ballesteros M, Negro MJ (2010) Pretreatment technologies for an efficient bioethanol production process based on enzymatic hydrolysis: a review. Bioresour Technol 101(13):4851–4861. doi:10.1016/j.biortech.2009.11.093
Blanch HW, Simmons BA, Klein-Marcuschamer D (2011) Biomass deconstruction to sugars. Biotechnol J 6(9):1086–1102. doi:10.1002/biot.201000180
Boonmanumsin P, Treeboobpha S, Jeamjumnunja K, Luengnaruemitchai A, Chaisuwan T, Wongkasemjit S (2012) Release of monomeric sugars from Miscanthus sinensis by microwave-assisted ammonia and phosphoric acid treatments. Bioresour Technol 103(1):425–431. doi:10.1016/j.biortech.2011.09.136
Brosse N, Sannigrahi P, Ragauskas A (2009) Pretreatment of miscanthus × giganteus using the ethanol organosolv process for ethanol production. Ind Eng Chem Res 48(18):8328–8334. doi:10.1021/Ie9006672
Brosse N, El Hage R, Sannigrahi P, Ragauskas A (2010) Dilute sulphuric acid and ethanol organosolv pretreatment of miscanthus × giganteus. Cellul Chem Technol 44(1–3):71–78
Brosse N, Dufour A, Meng X, Sun Q, Ragauskas A (2012) Miscanthus: a fast-growing crop for biofuels and chemicals production. Biofuels, Bioprod Biorefin 6(5):580–598. doi:10.1002/bbb.1353
Cao WX, Sun C, Liu RH, Yin RZ, Wu XW (2012) Comparison of the effects of five pretreatment methods on enhancing the enzymatic digestibility and ethanol production from sweet sorghum bagasse. Bioresour Technol 111:215–221. doi:10.1016/j.biortech.2012.02.034
Carroll A, Somerville C (2009) Cellulosic biofuels. Annu Rev Plant Biol 60:165–182. doi:10.1146/annurev.arplant.043008.092125
Cho NS, Matsumoto Y, Cho HY, Shin SJ, Ohga S (2008) Effect of urea addition on soda pulping of oak wood. J Fac Agric Kyushu Univ 53(1):1–5
Cochaux A, Crolet J, Aveni A, Robert A (1995) Use of amines in alkaline pulping: preparation of cellulosic pulps with high tearing strength. Cellul Chem Technol 29(3):339–360
de Vrije T, Bakker RR, Budde MAW, Lai MH, Mars AE, Claassen PAM (2009) Efficient hydrogen production from the lignocellulosic energy crop Miscanthus by the extreme thermophilic bacteria Caldicellulosiruptor saccharolyticus and Thermotoga neapolitana. Biotechnol Biofuels. doi:10.1186/1754-6834-2-12
El Hage R, Brosse N, Chrusciel L, Sanchez C, Sannigrahi P, Ragauskas A (2009) Characterization of milled wood lignin and ethanol organosolv lignin from miscanthus. Polym Degrad Stabil 94(10):1632–1638. doi:10.1016/j.polymdegradstab.2009.07.007
Elander RT, Dale BE, Holtzapple M, Ladisch MR, Lee YY, Mitchinson C, Saddler JN, Wyman CE (2009) Summary of findings from the biomass refining consortium for applied fundamentals and innovation (CAFI): corn stover pretreatment. Cellulose 16(4):649–659. doi:10.1007/s10570-009-9308-y
Geng XL, Henderson WA (2012) Pretreatment of corn stover by combining ionic liquid dissolution with alkali extraction. Biotechnol Bioeng 109(1):84–91. doi:10.1002/bit.23281
Ghose TK (1987) Measurement of cellulase activities. Pure Appl Chem 59(2):257–268
Gupta R, Lee YY (2010) Investigation of biomass degradation mechanism in pretreatment of switchgrass by aqueous ammonia and sodium hydroxide. Bioresour Technol 101(21):8185–8191. doi:10.1016/j.biortech.2010.05.039
Helmy SA, Aboustate MA (1993) Suitability of alkaline–ethanol–ethylenediamine solutions for producing viscose pulps. Cell Chem Technol 27(4):405–410
Ibáñez AB, Bauer S (2014) Downscaled method using glass microfiber filters for the determination of Klason lignin and structural carbohydrates. Biomass Bioenergy 68:75–81. doi:10.1016/j.biombioe.2014.06.013
Ingram LO, Geddes CC, Nieves IU (2011a) Advances in ethanol production. Curr Opin Biotech 22(3):312–319. doi:10.1016/j.copbio.2011.04.012
Ingram T, Wormeyer K, Lima JCI, Bockemuhl V, Antranikian G, Brunner G, Smirnova I (2011b) Comparison of different pretreatment methods for lignocellulosic materials. Part I: conversion of rye straw to valuable products. Bioresour Technol 102(8):5221–5228. doi:10.1016/j.biortech.2011.02.005
Ishikura Y (2011) Changes of wood properties treated with aqueous amine solution, bending tests and X-ray analysis of wood after amine treatment. J Mater Sci 46(11):3785–3791. doi:10.1007/s10853-011-5292-3
Jahan MS, Farouqui FI (2000) Pulping of whole jute plant (Corchorus capsularis) by soda-amine process. Holzforschung 54(6):625–630
Jahan MS, Farouqui FI (2002) Kinetics of jute pulping by soda-amine processes. Cell Chem Technol 36(3–4):357–366
Jordan DB, Bowman MJ, Braker JD, Dien BS, Hector RE, Lee CC, Mertens JA, Wagschal K (2012) Plant cell walls to ethanol. Biochem J 442:241–252. doi:10.1042/Bj20111922
Kim KH, Ko JK, Bak JS, Jung MW, Lee HJ, Choi IG, Kim TH (2009) Ethanol production from rice straw using optimized aqueous-ammonia soaking pretreatment and simultaneous saccharification and fermentation processes. Bioresour Technol 100(19):4374–4380. doi:10.1016/j.biortech.2009.04.026
Kim Y, Mosier NS, Ladisch MR, Pallapolu VR, Lee YY, Garlock R, Balan V, Dale BE, Donohoe BS, Vinzant TB, Elander RT, Falls M, Sierra R, Holtzapple MT, Shi J, Ebrik MA, Redmond T, Yang B, Wyman CE, Warner RE (2011) Comparative study on enzymatic digestibility of switchgrass varieties and harvests processed by leading pretreatment technologies. Bioresour Technol 102(24):11089–11096. doi:10.1016/j.biortech.2011.06.054
Klein-Marcuschamer D, Oleskowicz-Popiel P, Simmons BA, Blanch HW (2010) Technoeconomic analysis of biofuels: a wiki-based platform for lignocellulosic biorefineries. Biomass Bioenergy 34(12):1914–1921. doi:10.1016/j.biombioe.2010.07.033
Kumar R, Wyman CE (2009) Effect of enzyme supplementation at moderate cellulase loadings on initial glucose and xylose release from corn stover solids pretreated by leading technologies. Biotechnol Bioenergy 102(2):457–467. doi:10.1002/Bit.22068
Kumar P, Barrett DM, Delwiche MJ, Stroeve P (2009) Methods for pretreatment of lignocellulosic biomass for efficient hydrolysis and biofuel production. Ind Eng Chem Res 48(8):3713–3729. doi:10.1021/Ie801542g
Kurakake M, Kisaka W, Ouchi K, Komaki T (2001) Pretreatment with ammonia water for enzymatic hydrolysis of corn husk, bagasse, and switchgrass. Appl Biochem Biotech 90(3):251–259
Liu Z, Padmanabhan S, Cheng K, Schwyter P, Pauly M, Bell AT, Prausnitz JM (2013) Aqueous-ammonia delignification of miscanthus followed by enzymatic hydrolysis to sugars. Bioresour Technol 135:23–29. doi:10.1016/j.biortech.2012.10.133
Padmanabhan S, Kim M, Blanch HW, Prausnitz JM (2011) Solubility and rate of dissolution for Miscanthus in hydrophilic ionic liquids. Fluid Phase Equilibr 309(1):89–96. doi:10.1016/j.fluid.2011.06.034
Padmanabhan S, Zaia E, Wu K, Blanch HW, Clark DS, Bell AT, Prausnitz JM (2012) Delignification of Miscanthus by extraction. Sep Sci Technol 47(2):370–376. doi:10.1080/01496395.2011.629639
Park JC, Nguyen TAD, Kim KR, Han SJ, Cho HY, Kim JW, Park SM, Sim SJ (2010) Pretreatment of rice straw with ammonia and ionic liquid for lignocellulose conversion to fermentable sugars. Bioresour Technol 101(19):7432–7438. doi:10.1016/j.biortech.2010.04.053
Qing Q, Wyman CE (2011) Supplementation with xylanase and beta-xylosidase to reduce xylo-oligomer and xylan inhibition of enzymatic hydrolysis of cellulose and pretreated corn stover. Biotechnol Biofuels 4:18. doi:10.1186/1754-6834-4-18
Rodriguez A, Jimenez L (2008) Pulping with organic solvents other than alcohols. Afinidad 65(535):188–196
Rodriguez H, Padmanabhan S, Poon G, Prausnitz JM (2011) Addition of ammonia and/or oxygen to an ionic liquid for delignification of miscanthus. Bioresour Technol 102(17):7946–7952. doi:10.1016/j.biortech.2011.05.039
Sarwar MJ, Farouqui F, Abdullah IS (2001) Pulping of jute with amines. Cell Chem Technol 35(1–2):177–187
Shill K, Padmanabhan S, Xin Q, Prausnitz JM, Clark DS, Blanch HW (2011) ionic liquid pretreatment of cellulosic biomass: enzymatic hydrolysis and ionic liquid recycle. Biotechnol Bioeng 108(3):511–520. doi:10.1002/Bit.23014
Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D, Crocker D (2010) Determination of structural carbohydrates and lignin in biomass. http://www.nrel.gov/biomass/analytical_procedures.html
Sluiter JB, Ruiz RO, Scarlata CJ, Sluiter AD, Templeton DW (2010b) Compositional analysis of lignocellulosic feedstocks. 1. Review and description of methods. J Agr Food Chem 58(16):9043–9053. doi:10.1021/Jf1008023
Sousa LD, Chundawat SPS, Balan V, Dale BE (2009) ‘Cradle-to-grave’ assessment of existing lignocellulose pretreatment technologies. Curr Opin Biotech 20(3):339–347. doi:10.1016/j.copbio.2009.05.003
Sun RC, Sun YC, Wen JL, Xu F (2010) Fractional and structural characterization of organosolv and alkaline lignins from Tamarix austromogoliac. Sci Res Essays 5(24):3850–3864
Tao L, Aden A, Elander RT, Pallapolu VR, Lee YY, Garlock RJ, Balan V, Dale BE, Kim Y, Mosier NS, Ladisch MR, Falls M, Holtzapple MT, Sierra R, Shi J, Ebrik MA, Redmond T, Yang B, Wyman CE, Hames B, Thomas S, Warner RE (2011) Process and technoeconomic analysis of leading pretreatment technologies for lignocellulosic ethanol production using switchgrass. Bioresour Technol 102(24):11105–11114. doi:10.1016/j.biortech.2011.07.051
Templeton DW, Scarlata CJ, Sluiter JB, Wolfrum EJ (2010) Compositional analysis of lignocellulosic feedstocks. 2. Method uncertainties. J Agric Food Chem 58(16):9054–9062. doi:10.1021/Jf100807b
Wang Y, Spratling BM, Zobell DR, Wiedmeier RD, McAllister TA (2004) Effect of alkali pretreatment of wheat straw on the efficacy of exogenous fibrolytic enzymes. J Anim Sci 82(1):198–208
Wang ZG, Yokoyama T, Matsumoto Y (2010) Dissolution of ethylenediamine pretreated pulp with high lignin content in LiCl/DMSO without milling. J Wood Chem Technol 30(3):219–229. doi:10.1080/02773810903477613
Wang Z, Li R, Xu J, Marita JM, Hatfield RD, Qu R, Cheng JJ (2012) Sodium hydroxide pretreatment of genetically modified switchgrass for improved enzymatic release of sugars. Bioresour Technol 110:364–370
Wormeyer K, Ingram T, Saake B, Brunner G, Smirnova I (2011) Comparison of different pretreatment methods for lignocellulosic materials. Part II: influence of pretreatment on the properties of rye straw lignin. Bioresour Technol 102(5):4157–4164. doi:10.1016/j.biortech.2010.11.063
Wyman CE, Dale BE, Elander RT, Holtzapple M, Ladisch MR, Lee YY, Mitchinson C, Saddler JN (2009) Comparative sugar recovery and fermentation data following pretreatment of poplar wood by leading technologies. Biotechnol Prog 25(2):333–339. doi:10.1021/Bp.142
Wyman CE, Balan V, Dale BE, Elander RT, Falls M, Hames B, Holtzapple MT, Ladisch MR, Lee YY, Mosier N, Pallapolu VR, Shi J, Thomas SR, Warner RE (2011) Comparative data on effects of leading pretreatments and enzyme loadings and formulations on sugar yields from different switchgrass sources. Bioresour Technol 102(24):11052–11062. doi:10.1016/j.biortech.2011.06.069
Acknowledgments
The authors are grateful to the Energy Biosciences Institute (University of California, Berkeley) for the financial support and to Dr. Amit Gokhale and Dr.Waheed Afzal for fruitful discussions.
Author information
Authors and Affiliations
Corresponding authors
Ethics declarations
Conflict of interest
The authors declare that they have no conflict of interest in the publication.
Rights and permissions
Open Access This article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.
About this article
Cite this article
Padmanabhan, S., Schwyter, P., Liu, Z. et al. Delignification of miscanthus using ethylenediamine (EDA) with or without ammonia and subsequent enzymatic hydrolysis to sugars. 3 Biotech 6, 23 (2016). https://doi.org/10.1007/s13205-015-0344-z
Received:
Accepted:
Published:
DOI: https://doi.org/10.1007/s13205-015-0344-z