Switchable ionic liquids enable efficient nanofibrillation of wood pulp
Use of switchable ionic liquid (SIL) pulp offers an efficient and greener technology to produce nanofibers via ultrafine grinding. In this study, we demonstrate that SIL pulp opens up a mechanically efficient route to the nanofibrillation of wood pulp, thus providing both a low cost and chemically benign route to the production of cellulose nanofibers. The degree of fibrillation during the process was evaluated by viscosity and optical microscopy of SIL treated, bleached SIL treated and a reference pulp. Furthermore, films were prepared from the fibrillated material for characterization and tensile testing. It was observed that substantially improved mechanical properties were attained as a result of the grinding process, thus signifying nanofibrillation. Both SIL treated and bleached SIL treated pulps were fibrillated into nanofibers with fiber diameters below 15 nm thus forming networks of hydrophilic nature with an intact crystalline structure. Notably, it was found that the SIL pulp could be fibrillated more efficiently than traditional pulp since nanofibers could be produced with more than 30% less energy when compared to the reference pulp. Additionally, bleaching reduced the energy demand by further 16%. The study demonstrated that this switchable ionic liquid treatment has considerable potential in the commercial production of nanofibers due to the increased efficiency in fibrillation.
KeywordsSwitchable ionic liquids (SIL) Efficient fibrillation Wood pulp Cellulose nanofiber Ultrafine grinding
The utilization of the cellulose component of wood in various industrial processes would be greatly enhanced by the development of greener approaches to its fractionation. One such approach is the development of greener solvents for the extraction processes, such as deep eutectic solvents (Selkälä et al. 2016) and ionic liquids (Pang et al. 2016) to mention but a few. ‘Traditional’ ionic liquids (ILs) are a sub-class of molten salts composed of mainly organic cations and inorganic as well as organic anions, and frequently demonstrate melting points below the boiling point of water. More recently many families of more advanced ILs such as ‘switchable’ ILs have emerged (Anugwom et al. 2014b). Ionic liquids are interesting due to their tunable properties, rendering them suitable as solvents in many applications. Moreover, multitude of ionic liquids has high chemical and thermal stabilities and a wide liquidus range (Wasserscheid and Welton 2006). Several papers can be found in the literature that describes the use of conventional ionic liquids (ILs) in the fractionation of wood. Examples of such ionic liquids include 1-butyl-3-methylimidazolium chloride [C4MIM][Cl], (Swatloski et al. 2002) and 1-ethyl-3-methylimidazolium acetate [E2MIM][OAc], which in ionic liquid-mediated technology, have been reported as powerful when used to produce cellulose nanocrystals directly from wood (Abushammala et al. 2015).
However, the limitations associated with the use of conventional ionic liquids for biomass treatment are high cost, the use of precursors originating from fossil resources, multi-step industrial protocols and ambiguous recycling protocols for many of the formulations. These issues thus rendering them unattractive in large-scale processes. A typical drawback with them is the high viscosity of the wood-IL systems after dissolution, which makes recycling, recovery, and reuse of the ionic liquids less viable. Several recovery methods for ionic liquids used for biomass dissolution have been reported. These methods mainly involve the addition of an anti-solvent. The dissolved material can be precipitated out and the anti-solvent removed from the spent ionic liquid by evaporation (D’Andola et al. 2008; Varanasi et al. 2008). Switchable ionic liquids (SILs), on the other hand, are capable of ionic/non-ionic switching, for example, molecular-to-ionic switching by the addition or removal of a so called “trigger compound” (Anugwom et al. 2011; Jessop et al. 2005). It has been demonstrated in our earlier studies that SILs are potential novel solvents for fractionating lignocellulosic material into its various constituents (Anugwom et al. 2012a; Eta et al. 2014a, b). The power of SILs as solvents for biomass deconstruction was further strengthened when a new protocol, the short time high temperature (STHT) approach (Anugwom et al. 2014b) was carried out for delignification of lignocellulose biomass. The STHT approach was shown to be an efficient way to remove biomass lignin whereupon heavily diluted, aqueous solutions of switchable ionic liquids (SIL) as solvents were used to achieve an impressive delignification efficiency of 95 wt% (Anugwom et al. 2011). Further, the process was operated at low temperatures with a very short treatment time and at low wood-to-ionic solvent ratios. The solvent’s capacity for biomass deconstruction is the key to increasing process efficiency of the following mechanical processing of the pulp such as in the disintegration of the cellulose fibers to the nanoscale. Ultra-fine grinding techniques have been recognized as the most efficient approach in terms of energy consumed (Spence et al. 2011), and thus has great potential for the commercial, scaled-up production of nanofibers, since reduction of the processing energy is one of the most important prerequisites for industrial production. The aim of this study is to evaluate the use of switchable ionic liquids as a rapid, effective and chemical benign route to producing nanofibers from wood chips using ultrafine grinding.
Firstly, the fibrillation process of SIL treated wood pulp and a bleached SIL treated wood pulp to nanofibers is assessed and compared to that the fibrillation to nanofibers from a reference pulp, in this case a birch Kraft pulp. Secondly, the quality of the nanofibers produced was assessed by a comparison of their characteristics. To assess the fibrillation process, viscosity measurements and optical microscopy (OM) were used during the grinding process and mechanical properties of the films prepared from the fibrillated suspension were tested to evaluate the degree of separation. The energy consumption was also measured during the grinding process. The quality assessment of the nanofibers comprised of a study of the nuclear magnetic resonance spectroscopy (NMR) of the pulps before and after the treatment; the crystallinity of the materials before and after the fibrillation; the water contact angle and surface roughness the wood nanofiber films and the size distribution of the nanofibers characterized using atomic force microscope (AFM). Further to this, a chemical composition of the ionic liquid, SO2 switched DBU MEASIL derived birch pulp was studied before and after the treatment.
Hardwood birch (Betula pendula) in the form of chips was used as raw material for production of nanofibers and was provided by the Natural Resources Institute Finland, (Luke). The reference material was a commercial birch Kraft pulp provided by SCA (Munksund, SE). Used, as received, were the SIL precursors, 1,8-diazabicyclo-[5.4.0]-undec-7-ene (DBU, 99%) and monoethanol amine (MEA, 99%) from Sigma Aldrich and the SO2 (99.998%, H2O < 3 ppm) provided by AGA Oy (Linde group, Finland). The isopropyl alcohol (2-propanol) (Merck, 99%, USA) that was applied as the anti-solvent and for washing of the fractions. This was also used as received.
Synthesis of the switchable ionic liquid
Ionic liquid treatment of woody biomass in a non-stirred batch reactor
A 300 ml capacity batch autoclave (Parr Inc., USA) with an electric heater and an internal thermocouple was used in this study. 50 g of birch chips (approx. 2.3 cm × 8 cm), together with 250 g of SO2 switched DBU MEASIL and 150 ml of water were placed into the reactor to give a weight ratio of 1:5:3 of wood: SO2 DBU MEASIL: water. This was heated to 160 °C (433 K) for 2 h. No stirring was employed in order to avoid mechanical fibrillation of the chips during the treatment and consequent a low mixture viscosity could be maintained thus facilitating washing. It should also be mentioned that our earlier studies have shown that the process works well even in the absence of stirring. Upon completion of the treatment, the treated wood was subject to washing with a mixture of propanol and water until no visual evidence of the SIL could be found remaining in the solid fraction. This was further verified by testing for traces of sulphate ion in the filtrate using 10 vol% barium chloride. The SIL pulp samples were subsequently bleached and used for cellulose nanofiber production or used directly without bleaching. In neither case were the samples dried before use.
Bleaching of the SIL treated biomass was performed using acid chlorite bleaching following a previously described procedure by Anugwom et al. (2014a). Briefly a sample of 1 g was bleached with 0.8 g NaClO2 and 0.16 g AcOH in 40 ml water, at 75 °C for 2 h and the chemicals were added in two portions.
The SIL treated pulp was ground for a total duration of 150 min, compared to the bleached SIL pulp, which was processed for 70 min. The processing time in case of the reference pulp was 100 min. The energy consumption for the grinding process was established on the direct measurement of power using a power meter, Carlo Gavazzi, EM24 DIN (Italy) and the processing time. The energy demand was calculated from the product of power and time and expressed as MWh per dry weight ton of the nanofibers.
The samples were collected at regular intervals during the fibrillation process and characterized by viscosity measurements together with the optical microscope in order to assess the degree of fibrillation. The grinding process was stopped when a plateau in viscosity was reached and no larger structures could be observed by polarized microscope.
Preparation of films
Films containing various degrees of mechanical disintegration were prepared to assess the degree of fibrillation. After the grinding, the suspensions were adjusted to 0.2 wt% concentration and dispersed with a shear mixer, IKA T25, UltraTurrax, (IKA-Werke GmbH & Co., Germany), operated at 10,000 rpm for 10 min. The suspensions were then degassed and subsequently filtered with a membrane filter; pore size 0.45 µm, with a glass filter support. The wet cakes obtained were dried by hot pressing at 85 °C, using Fortune presses, LP300, (Fontijne Grotnes, The Netherlands), under 30 kPa for 40 min.
Chemical analysis: cellulose and hemicellulose content
The carbohydrate content of the samples was analyzed by gas chromatography (GC) after acid methanolysis, followed by silylation and acid hydrolysis followed by silylation to determine the hemicellulose and cellulose content of the sample, respectively (Sundberg et al. 1996; Willför et al. 2005; Anugwom et al. 2012b). For GC analysis, approximately 2 µl of the silylated sample was injected through a split injector (260 °C, split ratio 1:5) into a capillary column coated with dimethyl polysiloxane (HP-1, Hewlett Packard). The column length, internal diameter and film thickness were 30 m, 320 and 0.17 µm, respectively. The temperature program applied was a 4 °C/min ramp from 100 to 175 °C followed by 12 °C/min ramp from 175 to 290 °C. The detector (FID) temperature was 290 °C and hydrogen was used as the carrier gas. GC–MS (mass spectrometry) was used to identify the different peaks prior to the GC analysis.
Lignin content determination
The lignin content was determined using a modified method similar to the Klason lignin method but in which an autoclave treatment at 125 °C and 1.4 bar for 90 min is used to complete hydrolysis of polysaccharides instead of boiling for 4 h (Anugwom et al. 2012a; Schwanninger and Hinterstoisser 2002).
Nuclear magnetic resonance spectroscopy (NMR)
13C cross-polarization magic angle spinning (CP/MAS) experiments were performed on a Bruker 500 MHz Avance III spectrometer operating at a 13C frequency of 125.75 MHz and equipped with a 4 mm MAS probe. The SIL treated- and the reference pulp were analyzed as non-dried pulp but due to the high water content, the bleached SIL pulp was air-dried before analysis. 1 ms contact time was used and 4096 scans were collected for each sample at a spin rate of 10 kHz. The spectral data was processed with Topspin 3.2 software (Bruker Biospin, Germany) using a Gaussian window function. All spectra were recorded at ambient temperature.
Optical microscopy (OM)
The lateral dimensions of the raw materials, before the grinding process, were measured using a polarizing microscope, Nikon Eclipse LV100N POL (Japan) and the imaging software NIS-Elements D 4.30. The average values reported are based on 60 measurements of different fibers. The microstructure was also evaluated during the mechanical disintegration process.
Viscosity measurements were performed during the grinding using a Vibro Viscometer SV-10, (A&D Company, Ltd, Japan), at a constant shear rate. The velocity (shear rate) of the sensor plates is periodic and based on a sine-wave vibration with a frequency of 30 Hz and amplitude of <1 mm. The viscosity measurements were repeated once the temperature of the samples had been stabilized to 22.7 ± 1.0 °C to confirm that a plateau in viscosity had been reached during fibrillation. The presented values are an average of three measurements for each sample, where the samples were stirred between the measurements.
Atomic force microscopy (AFM)
The nanostructure was studied after the mechanical fibrillation for all samples using an Atomic Force Microscopy. The fibrillated sample suspension (0.01 wt%) was dispersed and deposited by spin coating onto a mica plate for imaging. The measurements were performed on a Veeco Multimode Scanning Probe, USA in tapping mode, with a tip model TESPA [antimony (n) doped Si], Bruker, USA. The nanofiber size (width) was measured from the height images using the Nanoscope V software and the size distribution presented are based on 40 different measurements for each sample. The size distributions were obtained by drawing a line across the height image and subsequently measuring all isolated nanofibers alongside this line. The procedure was repeated for several captured height images until 40 measurements were collected. AFM was also used for characterization of topographical features of the nanofiber films. The root-mean square roughness RMS values were measured from the height images. The images were flattened before the measurements to delete low frequency noise and remove tilt; no other image processing was performed. The values reported are the average of five different measurements on the surface area of 25 µm2. All measurements were conducted in air at room temperature.
Density and porosity
Scanning electron microscopy (SEM)
The morphologies of the films fracture surfaces were studied by SEM, JEOL, and JSM-IT300LV (USA) at an acceleration voltage of 10 kV. The samples were coated prior to the scanning using Bal-Tec MED 020 Coating system with a tungsten target to avoid charging.
The mechanical properties of the films networks structures, isolated after different processing times, were tested to provide an indication of the degree of fibrillation. Film samples cut to 40 mm in length and 5 mm in width were attached to paper frames to facilitate the mounting in the tensile machine. The tests were conducted using universal tensile testing equipment; AG X, (Shimadzu, Japan) equipped with 1 kN load cell. The tests were conducted at extension rate of 2 mm/min and the gauge length used was about 20 mm. Prior to experiments, all the samples were conditioned at 50 ± 2.0% relative humidity at 23 ± 1.0 °C for at least 24 h. The results are the average of at least eight sets of measurements.
X-ray diffraction (XRD)
Contact angle measurements
The water contact angle of the nanofibers films was measured using an EASYDROP contact angle measuring system with drop shape analysis DSA1 control and evaluation software (Krüss, Germany). A 4 µl drop of water was placed onto the sample and the software of the instrument calculated the contact angle over time with a sessile drop technique; the contact angle was determined immediately after a stable drop was formed on the sample surface and used for comparison of the nanofiber networks. The reported values are the average based on five measurements.
Results and discussion
Chemical composition of the DBUMEASO2SIL treated materials
After the SIL treatment using the Short Time-High temperature (STHT) approach (Anugwom et al. 2014b), a ~40 wt% reduction of the original weight was recorded after washing. The bleached and unbleached woody material after the SIL treatment was subjected to chemical analysis to determine its lignin, cellulose and hemicellulose contents, respectively. The result of the chemical analysis is given in Online Resource 1, together with the results for the reference pulp. The SIL treatment reduced the lignin content by 91 wt% compared to the total amount in the untreated wood, resulting in marginally lower lignin content than the reference pulp. The bleaching cycle further reduced the lignin content of the SIL treated wood to less than 2 wt%, thus half that of the lignin content of the SIL treated- and reference pulp. As shown previously, the SIL used was selective towards lignin dissolution (Anugwom et al. 2012a). The results of removal of hemicelluloses were similar in both the SIL treated- and the reference pulp. Bleaching combined with the SIL treatment further decreased the hemicellulose content (see Online Resource 1). In addition, the SIL treatment successfully removed over 90 wt% of the pectins and uronic acids from the wood.
Nuclear magnetic resonance spectroscopy (NMR) analysis
Lignin peaks usually appear in the region of 125–160 ppm with the exception of the methoxyl peak, which is located at 56 ppm. Signals from hemicelluloses overlap to a large extent with the cellulose peaks but presence of hemicellulose can be observed as a hump on the up-field side of the C1 peak from cellulose (Liitiä et al. 2003). Comparing the peak intensities of the different materials, it is clear that only small amounts of lignin and hemicellulose fractions are present, leaving only the cellulose peaks as the dominating features of the spectra (Fig. 3).
These results confirm the results from chemical analysis showing the SIL treated and bleached SIL contain minor amounts of hemicellulose. In addition, it is evident that the lignin still present after the SIL treatment gives rise to methoxyl resonances, which are no longer present after the subsequent bleaching process confirming the reduction in lignin. The presence of lignin in the reference material is not clearly seen in the spectra possibly reflecting the accuracy of NMR in detecting low lignin levels.
The larger woody structures observed for the SIL treated unground material appeared to require further a processing time of approximately 40 min to separate them before internal fibrillation could be initiated. However, in the bleached SIL, the initiation of internal fibrillation appeared much earlier and fibrillation was observed at the fiber ends after only 20 min of processing. After 40 min, comprehensive disintegration was observed for the bleached SIL. At 40 min, the reference material appears be at further stage of the disintegration than the SIL but not as advanced as the bleached SIL material.
The more rapid fibrillation for the bleached SIL pulp could be attributed to the combination of initially smaller fiber dimensions and lower lignin content. For the SIL treated and reference, the lignin may act to maintain the structural integrity of the fiber, thus resulting in a more gradual disintegration process, compared to the bleached SIL.
The AFM confirmed that the fibril dimensions were decreased from micro- to nanoscale upon the grinding process, though bundles of wood nanofibers also were observed in all materials. The height measurements of the isolated nanofibers was used to measure the widths of the nanofibers and had averaged values of 15 ± 8 nm for the SIL treated nanofibers, 12 ± 6 nm for the bleached SIL, and in case of the reference 14 ± 6 nm was measured. Thus, no significant differences could be confirmed in the size of the nanofibers in the final nanofiber gels when inspected on this scale and it can be tentatively concluded that the different processing routes and resulting different chemical composition appeared to have minor, if any effect on the nanofiber sizes. However, it should be noted that in AFM measurement, the field of is view visualized is restricted and thus larger structures are often overlooked (Chinga-Carrasco 2013).
The viscosity of the suspensions increased significantly during the mechanical separation and a gel formation was observed. This increase in viscosity is due to the fibrillation process leading to a greater exposure of the surface area of swollen fibrils, promoting more fibril-to-fibril bonding and this, in turn, implies a higher degree of fibrillation. The apparent increase in the viscosity with the progress of the fibrillation process could be seen of all pulps and has been previously reported for grinding of different wood pulps (Lahtinen et al. 2014). The viscosity increase in case of the bleached SIL pulp occurs almost immediately. The gradient is substantially lower for the SIL treated and reference pulp, yet the reference shows the highest maximum viscosity value. The lower gradient observed for the SIL treated pulp despite the fact that the concentration was in fact higher for this pulp. This is best explained by the breakdown of larger structures before gel formation was induced.
Fiber film characteristics
Large structures were clearly seen in the film from unground SIL treated pulp and the resulting porosity was 53 vol%. It also had a brown color, which we presume was from the remaining lignin in the SIL treated material. After fibrillation, the films of the material decreased in porosity to 21 vol% as the nanofibers pack closer than the larger microfibers, which was observed by SEM of the film fracture surface. The unground bleached SIL pulp films had a porosity at 46 vol% and thus lower than is unbleached counterpart. After fibrillation, the bleached SIL film porosity decreased to 19 vol% which is in similar to both the unbleached and reference nanofiber materials, the latter having a porosity of 59 vol% of the unground film and a final film porosity of 22 vol%. The slightly lower porosity obtained for the bleached SIL film was consistent with the more transparent appearance of the film. The porosity was decreased by about 70 wt% for all films upon the fibrillation process and their morphology showed more closely packed layered structures.
Both SIL treated samples reached a remarkably higher stress region and the bleaching resulted in further improvement of strain-to-failure compared to the reference material. An increase in the mechanical properties could be seen for all the fibrillated wood pulps, associated with the porosity decrease, owing to the smaller fiber dimensions which, in turn, results in the formation of more inter-fiber bonds (Nair et al. 2014) thus giving higher strength wood nanofiber networks. The SIL nanofibers do not reach the strength or strain-to-failure of the bleached materials. The remaining lignin may constitute a barrier for the formation of hydrogen bonds between cellulose molecules, mainly due to its more hydrophobic nature compared to cellulose (Shao and Li 2007), this would thus reduce the inter-fiber bonding and lower the strength for the SIL films. However, the results of the reference material which have nearly equivalent amount of both lignin and hemicellulose do not support this as it displayed a network with 20% higher strength, and 30% higher strain-to-failure than the network of SIL nanofibers. This suggests other reasons for reduced inter-fiber bonding in the SIL nanofiber networks such as either the material is less fibrillated or that the residual lignin yielding the brown color has a different effect on the network properties i.e. there is a difference in its surface chemistry compared to the remaining lignin in the reference material. The two possibilities are supported by the results of the bleached SIL nanofibers which displayed a 10% higher strength and about 20% increase in the strain-to-failure, and has a reduced lignin content of about 60 wt% compared to the SIL nanofibers and a rapid disintegration of the larger wood structures in the fibrillation process.
For the fibrillation process of the wood pulps into nanofibers, the amount of energy consumed (see Fig. 9) for the SIL treated pulp was 9 MWh/ton and, after bleaching, the energy consumption was further lowered to only 7 MWh/ton. The energy demand for the processing of the reference pulp was measured as 13 MWh/ton. Thus, the bleached SIL pulp could be fibrillated with almost half of the energy demand required for the reference material. In addition, the initial fibrillation appears more efficient for the bleached samples, an observation that may be attributed to the larger structures observed in the non-bleached SIL pulp, which require more energy to be disintegrated.
Interestingly, a more than 20% higher elastic modulus (Fig. 9b) was obtained in case of the bleached SIL nanofiber network with shortest processing time (1 h). Furthermore, a plateau appeared to have been reached for strength Fig. 9a, strain Fig. 9c and density Fig. 9d of the bleached SIL films. Nair et al. (2014) observed a similar behaviour of a plateau when grinding bleached softwood; however, this was reached after 4 h of grinding for strength and strain and 6 h for the density. A plausibly explanation for the bleached SIL treated pulp resulting in the most efficient fibrillation is that the large structures remaining in the SIL treated pulp are separated during the bleaching as the remaining lignin is removed, thus enabling a more direct fibrillation in the beginning of the ultrafine grinding process.
The crystallinity index of wood pulp and nanofibers, respectively
Wood pulp (%)
The use of different techniques for the determination of the crystallinity index renders it difficult to compare results with between studies since large variations between the use of different methods and baseline corrections has been shown (Park et al. 2010). Still, the values estimated in this study before and after the fibrillation are slightly lower to values reported, namely 86 and 90% for wood pulp and nanofibers, respectively, when fibrillated using grinding (Panthapulakkal and Sain 2012). However, it should be noted that the peak height method used in this study for estimation of the crystallinity index has been shown to underestimate the amorphous proportion, hence overestimating the relative amount of crystalline cellulose (Park et al. 2010). For this reason, the crystallinity index values in Table 1 should only be used for comparison between the samples. The results indicate that no dissolution of cellulose occurred during the SIL treatment, displaying cellulose I crystalline structure. The crystallinity index values were comparable to each other further indicating that neither the SIL treatment nor the grinding degrades the crystalline structures of the cellulose nanofibers with the processing conditions used in this study.
AFM amplitude images the nanofibers films derived from SIL-, bleached SIL-, and reference pulps
RMS roughness (nm)
Contact angle (°)
81 ± 5.6
60 ± 3.0
59 ± 10
54 ± 2.1
70 ± 4.0
62 ± 2.3
All the nanofibers showed hydrophilic nature with contact angles lower than 90°. Spence et al. (2010) showed that an increased contact angle value is associated with higher lignin content in wood pulps. Since lignin is less hydrophilic than cellulose, higher contact angles of the wood nanofibers films from SIL- and reference pulp were expected. The results did indeed follow this behavior and higher contact angles were found for SIL nanofibers and reference nanofibers, namely 60° and 62° respectively, compared to 54° for the bleached SIL nanofibers which has the lowest lignin content. It is also known that the water contact angle correlates with the topographical structure of the surface (Herrera et al. 2014). However, in this case any influence that the surface roughness has on the contact angle cannot be distinguished as significant, when the standard deviations are taken into account.
Switchable ionic liquid (SIL) processing was demonstrated as having a high commercial potential for pulping wood prior to mechanical fibrillation into nanofibers.
The SIL treatment drastically reduced the energy demand of obtaining nanofibers with diameters measured below 15 nm and intact crystalline structures with ultrafine grinding.
Furthermore, the porosity of the films made from the materials decreased by 70 wt% after fibrillation and an associated increase in the network strength was observed. In addition, a high elastic modulus was shown for the SIL nanofiber films at 9.6 and 12.4 GPa for the bleached SIL films. Bleached SIL nanofiber films have strength matching that of other nanofiber materials from ultrafine grinding. However, SIL nanofiber films were found to have a slightly lower strength.
The reduced energy demand (more than 30%) was achieved when SIL treated pulp was used compared to the reference pulp upon fibrillation through grinding. Additionally, bleaching reduced the energy consumption a further 16%.
Thus, bleached SIL pulp can yield nanofibers with virtually half the energy consumption compared to the bleached reference pulp, which together with the benign natural of the chemicals and the potential ease of solvent recycling render the commercial operations for the production of nanofibers much more realistic.
The authors would like to acknowledge the financial support under Bio4Energy—a strategic research environment appointed by the Swedish government, Wallenberg Wood Science Center (WWSC) and Nordic Forest research (SNS) WoodPro.
Compliance with ethical standards
Conflicts of interest
The authors declare that they have no conflict of interest.
- Aitomäki Y, Moreno-Rodriguez S, Lundström S, Oksman K (2015) Vacuum infusion of nanocellulose networks of different porosity. In: Proceedings of the 20th international conference on composite materials, Copenhagen, DenmarkGoogle Scholar
- D’Andola G, Szarvas L, Massonne K, Stegmann V (2008) Ionic liquids for solubilization of polymers. WO Patent 2008/043837Google Scholar
- Varanasi S, Shall AC, Dado P A, Anderson J, Rao K, Paripati P (2008) Biomass pretreatment. WO Patent 2008/11291A2Google Scholar
- Wasserscheid P, Welton T (2006) Ionic liquids in synthesis. Wiley, WeinheimGoogle Scholar
Open AccessThis 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.