Ionic liquid pretreatment of cellulosic biomass: enzymatic hydrolysis and ionic liquid recycle

Ionic liquids (ILs) are promising solvents for the pretreatment of biomass as certain ILs are able to completely solubilize lignocellulose. The cellulose can readily be precipitated with an anti-solvent for further hydrolysis to glucose, but the anti-solvent must be removed for the IL to be recovered and recycled. We describe the use of aqueous kosmotropic salt solutions to form a three-phase system that precipitates the biomass, forming IL-rich and salt-rich phases. The phase behavior of [Emim][Ac] and aqueous phosphate salt systems is presented, together with a process for recycling the [Emim][Ac] and enzymatically hydrolyzing the cellulose. This process reduces the amount of water to be evaporated from recycled IL, permitting efficient recycle of the IL. Material balances on the process, with multiple recycles of the [Emim][Ac], quantify the major components from a Miscanthus feedstock through the pretreatment, separation, and enzymatic hydrolysis steps. A more rapid and higher yielding conversion of cellulose to glucose is obtained by use of the three-phase system as compared to the cellulose obtained from biomass pretreated with IL and precipitated with water. The addition of a kosmotropic salt during the precipitation results in partial delignification of the biomass, which makes the substrate more accessible, enhancing the enzymatic hydrolysis.     

The study of factors affecting the enzymatic hydrolysis of cellulose after ionic liquid pretreatment

Cellulose resource has got much attention as a promising replacement of fossil fuel. The hydrolysis of cellulose is the key step to chemical product and liquid transportation fuel. In this paper a serials of chloride, acetate, and formate based ionic liquids were used as solvents to dissolve cellulose. The cellulose regenerated from ILs was characterized by FTIR and X-ray powder diffraction. From the characterization and analysis, it was found that the original close and compact structure has changed a lot. After enzymatic hydrolysis, different kinds of ionic liquids (ILs) have different yields of the reducing sugar (TRS). They are 100%, 90.72%, and 88.92% from 1-butyl-3-methylimidazolium chloride ([BMIM]Cl), 1-ethyl-3-methylimidazolium acetate ([EMIM][OAc]), 1-butyl-3-methylimidazolium formate ([BMIM][HCOO]) respectively after enzymatic hydrolysis at 50 °C for 5 h. The results indicated that the yields and the hydrolysis rates were improved apparently after ILs pretreatment comparing with the untreated substrates.     

Gamma-ray irradiation as a pretreatment for the enzymatic hydrolysis of cellulose

Summary The susceptibility of cellulose to enzymatic hydrolysis can be significantly affected through pretreatment by means of gamma-ray radiation. Experiments were carried out to investigate the effects of this radiation on enzymatic hydrolysis and on the two major structural features of cellulose that most influence hydrolysis, namely, specific surface area and crystallinity.D. H. Beardmore is currently with Phillips Petroleum Company, Bartlesville, OK 74004, U.S.A.     

Kinetic modeling of rapid enzymatic hydrolysis of crystalline cellulose after pretreatment by NMMO

Pretreatment of cellulose with an industrial cellulosic solvent, N-methylmorpholine-N-oxide, showed promising results in increasing the rate of subsequent enzymatic hydrolysis. Cotton linter was used as high crystalline cellulose. After the pretreatment, the cellulose was almost completely hydrolyzed in less than 12 h, using low enzyme loading (15 FPU/g cellulose). The pretreatment significantly decreased the total crystallinity of cellulose from 7.1 to 3.3, and drastically increased the enzyme adsorption capacity of cellulose by approximately 42 times. A semi-mechanistic model was used to describe the relationship between the cellulose concentration and the enzyme loading. In this model, two reactions for heterogeneous reaction of cellulose to glucose and cellobiose, and a homogenous reaction for cellobiose conversion to glucose was incorporated. The Langmuir model was applied to model the adsorption of cellulase onto the treated cellulose. The competitive inhibition was also considered for the effects of sugar inhibition on the rate of enzymatic hydrolysis. The kinetic parameters of the model were estimated by experimental results and evaluated.     

Visualization of biomass solubilization and cellulose regeneration during ionic liquid pretreatment of switchgrass

Auto‐fluorescent mapping of plant cell walls was used to visualize cellulose and lignin in pristine switchgrass (Panicum virgatum) stems to determine the mechanisms of biomass dissolution during ionic liquid pretreatment. The addition of ground switchgrass to the ionic liquid 1‐n‐ethyl‐3‐methylimidazolium acetate resulted in the disruption and solubilization of the plant cell wall at mild temperatures. Swelling of the plant cell wall, attributed to disruption of inter‐ and intramolecular hydrogen bonding between cellulose fibrils and lignin, followed by complete dissolution of biomass, was observed without using imaging techniques that require staining, embedding, and processing of biomass. Subsequent cellulose regeneration via the addition of an anti‐solvent, such as water, was observed in situ and provided direct evidence of significant rejection of lignin from the recovered polysaccharides. This observation was confirmed by chemical analysis of the regenerated cellulose. In comparison to untreated biomass, ionic liquid pretreated biomass produces cellulose that is efficiently hydrolyzed with commercial cellulase cocktail with high sugar yields over a relatively short time interval. Biotechnol. Bioeng. 2009; 104: 68–75 Published 2009 Wiley Periodicals, Inc.     

Reconstitution of cellulose and lignin after [C2mim][OAc] pretreatment and its relation to enzymatic hydrolysis

Although the effects of cellulose crystallinity and lignin content as two major structural features on enzymatic hydrolysis have been extensively studied, debates regarding their effects still exist. In this study, reconstitution of cellulose and lignin after 1‐ethyl‐3‐methylimidazolium acetate ([C₂mim][OAc]) pretreatment was proposed as a new method to study their effects on enzymatic digestibility. Different mechanisms of lignin content for reduction of cellulose hydrolysis were found between the proposed method and the traditional method (mixing of cellulose and lignin). The results indicated that a slight change of the crystallinity of the reconstituted materials may play a minor role in the change of enzyme efficiency. In addition, the present study suggested that the lignin content does not significantly affect the digestibility of cellulose, whereas the conversion of cellulose fibers from the cellulose I to the cellulose II crystal phase plays an important role when an ionic liquid pretreatment of biomass was conducted. Biotechnol. Bioeng. 2013; 110: 729–736. © 2012 Wiley Periodicals, Inc.     

Structural comparison and enhanced enzymatic hydrolysis of eucalyptus cellulose via pretreatment with different ionic liquids and catalysts

Eucalyptus was fractionated with mild alkaline process, and the obtained cellulose fraction was pretreated with various ionic liquids (ILs) to enhance the enzymatic saccharification. The results showed that the ILs used was efficient for the hydrolysis of cellulose, with the maximum total reducing sugars (TRS) yield over 80% at 50 °C. The regenerated cellulose substrate exhibited a significant improvement about 4.4–6.4 folds enhancement on saccharification rate during the first 4 h reaction. The crystallinity index (CrI) of cellulose via 1-ally-3-methylimidazolium ([AMIM]Cl) pretreatment was significantly decreased from 70.2% to 31.2%, resulting in structural change from cellulose I to cellulose II, which enabled the cellulase enzymes easier access to hydrolyze cellulose. However, 1-butyl-3methylimidazolium acesulfamate ([BMIM]Ace) pretreatment had no large effect on the CrI although a high conversion yield in glucose was obtained. The surface morphologies of the regenerated substrate which was pretreated via 1-butyl-3-methylimidazolium chloride ([BMIM]Cl) and 1-ethyl-3-methylimidazolium acetate ([EMIM]Ac) showed more porous and incompact network of cellulose when compared with the untreated substrate. This result indicated a better accessibility by cellulases to the cellulose surface. Besides, a certain amount of catalysts such as MgCl₂ and H₂SO₄ could improve the rate of enzymatic saccharification.     

Effects of organosolv pretreatment and enzymatic hydrolysis on cellulose structure and crystallinity in Loblolly pine

Ethanol organosolv pretreatment was performed on Loblolly pine to enhance the efficiency of enzymatic hydrolysis of cellulose to glucose. Solid-state ¹³C NMR spectroscopy coupled with line shape analysis was used to determine the structure and crystallinity of cellulose isolated from pretreated and enzyme-hydrolyzed Loblolly pine. The results indicate reduced crystallinity of the cellulose following the organosolv pretreatment, which renders the substrate easily hydrolyzable by cellulase. The degree of crystallinity increases and the relative proportion of para-crystalline and amorphous cellulose decreases after enzymatic hydrolysis, indicating preferential hydrolysis of these regions by cellulase. The structural and compositional changes in this material resulting from the organosolv pretreatment and cellulase enzyme hydrolysis of the pretreated wood were studied with solid-state CP/MAS ¹³C NMR spectroscopy. NMR spectra of the solid material before and after the treatments show that hemicelluloses and lignin are degraded during the organosolv pretreatment.     

Comparison of steam and ammonia pretreatment for enzymatic hydrolysis of cellulose

Summary Aspenwood, wheat straw, wheat chaff and alfalfa stems were treated under pressure with either steam or ammonia. The material was then water or methanol/water extracted. The extent of enzymatic hydrolysis of the cellulose portion of the treated substrates was compared using two different cellulases, a commercial preparation, Celluclast, and those from the fungus Trichoderma harzianum. Both steam and ammonia treatment enhanced the accessibility of the cellulose as measured by hydrolysis. Methanol extraction of steamed material generally reduced the access of the enzyme to the cellulose, whereas methanol extraction of ammonia-treated material increased accessibility. The optimum combinations of pretreatment and extraction method depended on the substrate and on the enzyme system; no treatment suitable for all situations could be selected.     

Partial acid hydrolysis of cellulosic materials as a pretreatment for enzymatic hydrolysis

Partial acid hydrolysis was studied as a per treatment to enhance enzymatic hydrolysis, such a pretreatment was carried out in a continuous flow reactor on oak corn Stover, newsprint, and Solka Floc at temperatures ranging from 160 to 220°C, acid concentration ranging from 0 to 1.2%, and a fixed treatment time of 0.22 min. The resulting slurries and solids were than hydrolyzed with Trichoderma ressei QM 9414 cellulase at 50°C for 48 hr. For all substrates except Solka Floc, increased glucose yields were achieved during enzymatic hydrolysis of the pretreated materials as compared to hydrolysis of the original substrate. In several cases, after pretreatment, 100° of the potential glucose content of the substrate was converted to glucose after 24hr of enzymatic hydrolysis. It is felt that the increased glucose yields achieved after this pretreatment are due to acid's removal of hemicellulose, reduced degree of polymerization, and possibly due to a change in the crystal structure of the cellulose.     

Solid acid and microwave-assisted hydrolysis of cellulose in ionic liquid

Solid acid-catalyzed hydrolysis of cellulose in ionic liquid was greatly promoted by microwave heating. H-form zeolites with a lower Si/Al molar ratio and a larger surface area showed a relatively higher catalytic activity. These solid catalysts exhibited better performance than the sulfated ion-exchanging resin NKC-9. Compared with conventional oil bath heating mode, microwave irradiation at an appropriate power significantly reduced the reaction time and increased the yields of reducing sugars. A typical hydrolysis reaction with Avicel cellulose produced glucose in around 37% yield within 8 min.     

Enhanced stability and activity of cellulase in an ionic liquid and the effect of pretreatment on cellulose hydrolysis

We discuss the hydrolysis of cellulose using a pure cellulase: endo-1,4-β-D-glucanase (EG) from the fungus, Aspergillus niger, in buffer, the pure ionic liquid (IL), tris-(2-hydroxyethyl)-methylammonium methylsulfate (HEMA), and various mixtures of the two at different temperatures. Steady-state fluorescence and absorbance studies were performed to monitor the stability and activity of EG using cellulose azure as the substrate. EG attains its highest activity at 45°C in buffer and denatures at ～55°C. On the other hand, HEMA imparts substantial stability to the enzyme, permitting the activity to peak at 75°C. The relative roles of temperature, viscosity, pH, polarity, and the constituent ions of the ILs on the hydrolysis reaction are examined. It is demonstrated that pretreatment of cellulose with ILs such as BMIM Cl, MIM Cl, and HEMA results in more rapid conversion to glucose than hydrolysis with cellulose that is not pretreated. The percent conversion to glucose from pretreated cellulose is increased when the temperature is increased from 45 to 60°C. Two different ILs are used to increase the efficiency of cellulose conversion to glucose. Cellulose is pretreated with BMIM Cl. Subsequent hydrolysis of the pretreated cellulose in 10-20% solutions of HEMA in buffer provides higher yields of glucose at 60°C. Finally, to our knowledge, this is the first study dealing with a pure endoglucanase from commercial A. niger. This enzyme not only shows higher tolerance to ILs, such as HEMA, but also has enhanced thermostability in the presence of the IL.     

Products of enzymatic hydrolysis of cellulose and its derivatives

Cellobiose and glucose were determined in a mixture of the two carbohydrates by methods involving the use of glucose oxidase and of β-glucosidase.Paper-partition chromatography is used as a confirmatory method in the identification of the hydrolysis products and in the detection of the various constituents.The cellulolytic organisms studied produce large amounts of the enzyme Cx, which diffuses into the medium. Only small amounts of β-glucosidase are found outside the cell. Cellobiose resulting from Cx activity can enter the cells as rapidly as can glucose.The role of cellobiose as a principal product in the hydrolysis of cellulose is confirmed. It is hypothesized that the principal final product of Cx activity is cellobiose, and that the presence of cellobiase in the medium is not a prerequisite to utilization of cellobiose by the organism. This is a correction of the hypothesis previously published stating that glucose appeared to be the final product of Cx activity.     

Cellulase kinetics as a function of cellulose pretreatment

Microcrystalline cellulose (Avicel) was subjected to three different pretreatments (acid, alkaline, and organosolv) before exposure to a mixture of cellulases (Celluclast). Addition of beta-glucosidase, to avoid the well-known inhibition of cellulase by cellobiose, markedly accelerated cellulose hydrolysis up to a ratio of activity units (beta-glucosidase/cellulase) of 20. All pretreatment protocols of Avicel were found to slightly increase its degree of crystallinity in comparison with the untreated control. Adsorption of both cellulase and beta-glucosidase on cellulose is significant and also strongly depends on the wall material of the reactor. The conversion-time behavior of all four states of Avicel was found to be very similar. Jamming of adjacent cellulase enzymes when adsorbed on microcrystalline cellulose surface is evident at higher concentrations of enzyme, beyond 400 U/L cellulase/8 kU/L beta-glucosidase. Jamming explains the observed and well-known dramatically slowing rate of cellulose hydrolysis at high degrees of conversion. In contrast to the enzyme concentration, neither the method of pretreatment nor the presence or absence of presumed fractal kinetics has an effect on the calculated jamming parameter for cellulose hydrolysis.     

Improving enzymatic hydrolysis of wheat straw using ionic liquid 1-ethyl-3-methyl imidazolium diethyl phosphate pretreatment

This study aims to establish a cellulose pretreatment process using ionic liquids (ILs) for efficient enzymatic hydrolysis. The IL 1-ethyl-3-methyl imidazolium diethyl phosphate ([EMIM]DEP) was selected in view of its low viscous and the potential of accelerating enzymatic hydrolysis, and it could be recyclable. The yield of reducing sugars from wheat straw pretreated with this IL at 130 °C for 30 min reached 54.8% after being enzymatically hydrolyzed for 12 h. Wheat straw regenerated were hydrolyzed more easily than that treated with water. The fermentability of the hydrolyzates, obtained after enzymatic saccharification of the regenerated wheat straw, was evaluated using Saccharomyces cerevisiae. This microbe could ferment glucose efficiently, and the ethanol production was 0.43 g/g glucose within 26 h. In conclusion, the IL [EMIM]DEP shows promise as pretreatment solvent for wheat straw, although its cost should be reduced and in-depth exploration of this subject is needed.     

Properties of a reversible soluble-insoluble cellulase and its application to repeated hydrolysis of crystalline cellulose

Cellulase was covalently immobilized on an enteric coating polymer, Eudragit L, that is reversibly soluble and insoluble depending on the pH of the medium. The hydrolysis of solid cellulose with the immobilized enzyme can take advantage of the soluble property of the immobilized enzyme itself at the most reactive pH value; on the other hand, recovery of the enzyme can take advantage of the insoluble property of the enzyme at other pH values. It was experimentally confirmed that 100% of immobilized enzyme activity in solution can be recovered by precipitation and by dissolving it again by alternative change of pH. After a period of hydrolysis, immobilized enzyme and unreacted cellulose were precipitated together to remove the product-the soluble sugar solution-by changing pH. Following this, a new buffer solution was added to the precipitate to dissolve it and resume the reaction. This was repeated several times. The hydrolysis rate of this process increased significantly compared with that of a batch process. Utilization of the reversible soluble-insoluble carrier for immobilizing enzyme is promising, not only for cellulose-cellulase systems, but also for other heterogeneous reaction systems.     

Mild pretreatment and enzymatic saccharification of cellulose with recycled ionic liquids towards one-batch process

The development of second-generation bioethanol involves minimizing the energy input throughout the processing steps. We report here that efficient ionic liquid pretreatments of cellulose can be achieved with short duration times (20min) at mild temperature (45°C) with [Emim](+)[MeO(H)PO(2)](-) and at room temperature (25°C) with [Emim](+)[CH(3)COO](-). In these conditions, yields of glucose were increased by a factor of 3. In addition, the recycling of these two imidazolium-based ILs can be performed in maintaining their efficiency to pretreat cellulose. The short time and mild temperature of cellulose solubilization allowed a one-batch processing of [Emim](+)[MeO(H)PO(2)](-) IL-pretreatment and saccharification. In the range from 0 to 100% IL in an aqueous enzymatic medium, the glucose yields were improved at IL proportions between 10 and 40%. The maximum yield at 10% IL is very promising to consider one batch process as efficient as two-step process.