Cellulose-based fiber spinning processes using ionic liquids

Cellulose, a natural, renewable, and environment friendly biopolymer, has been considered as a sustainable feedstock in the near future. However, only 0.3% of cellulose is today processed since it is not soluble in conventional solvents due to the strong hydrogen bonding network and highly ordered structure. Hence, the search of effective and eco-friendly solvents for cellulose dissolution has been a key pillar for decades. In the recent years, ionic liquids (ILs) have been proposed as green solvents for cellulose and have been applied for the production of cellulose-based fibers. This review aims to focus the attention toward fiber spinning methods of cellulose based on ILs, as well as recent progress in cellulose dissolution using ILs. Moreover, the development of cellulosic fibers blended with other biopolymers, and cellulose composites are presented. Finally, different applications of cellulose fibers and composites are summarized and discussed.


Introduction
Environmental issues related to the use of fossil-fuelbased materials, such as green gas emissions, human health impacts, among others, have encouraged researchers to replace petroleum-derived products with sustainable nature-friendly materials. In view of this, cellulose is one of the most abundant natural resources on earth, harvested from plants, animals, and bacteria, which can be easily processed and fairly functionalized. Nearly one trillion tons of the world annual biomass production is based on cellulose fibers or derivatives and, to date, cellulose has played a relevant role in the growth of numerous eco-friendly materials, which can affect (bio) economy in the future. Cellulose is considered as an infinite source of feedstock for the growing demand for environmentally friendly materials since it is regularly regenerated by nature in relatively short periods Abstract Cellulose, a natural, renewable, and environment friendly biopolymer, has been considered as a sustainable feedstock in the near future. However, only 0.3% of cellulose is today processed since it is not soluble in conventional solvents due to the strong hydrogen bonding network and highly ordered structure. Hence, the search of effective and eco-friendly solvents for cellulose dissolution has been a key pillar for decades. In the recent years, ionic liquids (ILs) have been proposed as green solvents for cellulose and have been applied for the production of cellulose-based fibers. This review aims to focus the of time (Brinchi et al. 2013). As a polysaccharide, cellulose has several desired features for (bio)engineering applications, such as hydrophilicity, biocompatibility, biodegradability, and proper mechanical properties (tensile strength ~ 120 MPa and Young's modulus ~ 2 GPa). Cellulose fibrils include crystalline and amorphous segments. Cellulose nanocrystals (CNC) and cellulose nanofibers (CNF) can be generated using chemical treatments and mechanical processes, respectively, which can be considered as two main categories of plant-derived nano-cellulose (NC) (Moon et al. 2011). Aiming at developing new functionalities and to attaining a variety of environmental and social goals, there has been a relevant interest in producing continuous fibers from bio-based materials ( Fig. 1).
Hence, considerable attempts have been made to investigate the spinning of continuous fibers from cellulose to nano-cellulose. Cellulose fibers have been produced from cellulose solutions for more than hundred years (Woodings 2001). Although they have been applied in textiles traditionally, the interest in using them as polymeric reinforcements has also increased (Adusumali et al. 2006;Ganster and Fink 2006). These fibers are more attractive than other natural fibers (e.g., flax), due to their lower variability in fiber length, morphology and biochemical composition of the plant. Man-made cellulose fibers are produced by pursuing different methods that include a first dissolution followed by the actual process. Although the production of pure cellulose fibers is still challenging, wet-, dry-, dry-jet-wet and electrospinning techniques have been successfully used as procedures to produce continuous cellulose fibers in micro-and nano-dimensions. In fact, cellulose is scarcely soluble in common solvents due to the extensive inter-and/or intra-molecular hydrogen bonding. In addition to its low solubility, cellulose is also not meltable and, thus, it is impossible to use the meltspinning technique. Therefore, cellulose processing has required either a chemical derivatization or a physical dissolution in appropriate solvents.
Viscose and Lyocell procedures are currently the only two technologies that have been industrially developed for the generation of manmade cellulosic fibers. Nevertheless, they show issues related to the applied solvents within the cellulose dissolution stage. For example, during the viscose procedure, the use of highly toxic chemicals and the formation of gases can be harmful for workers and the environment. Hence, environmental pollution and safety costs have become a serious concern. For the N-methyl morpholine-N-oxide (NMMO monohydrate)-based Lyocell process that is now Fig. 1 Schematic illustration of the topics presented in this review article: cellulose from different sources as a sustainable naturefriendly material the only commercialized alternative to the spinning process of Viscose, there are also several limitations, such as poor thermal stability of the solvent, degradation of both the solvent and the cellulose due to the formation of by-products which require a large amount of stabilizers, high safety costs, complex dissolving techniques, serious solvent recovery procedures, and low productivity due to the low solubility of cellulose in the solvent (Rosenau et al. 2002(Rosenau et al. , 1999(Rosenau et al. , 2001. Owing to high-market demand for bio-based textiles and sustainable fashion products, the development of green spinning technologies is essential for the production of man-made cellulosic fibers. Practically, this requires the finding of green solvents that can dissolve raw celluloses effectively (Meksi and Moussa 2017).
Recently, room-temperature ionic liquids (ILs) have emerged as interesting green solvents that can efficiently dissolve and process biopolymers, such as silk (Goujon et al. 2012), wool (Zheng et al. 2015), chitin (Shamshina 2019), chitosan (Xie et al. 2006), lignocelluloses (Asim et al. 2019), wood, and cellulose (Morais et al. 2020). By virtue of their advantages, such as high dissolving ability, based on disruption of the hydrogen bond pattern present in the native polysaccharide (Pinkert et al. 2009), low vapor pressure (Welton 2018), chemical  and thermal stability (Maton et al. 2013), non-flammability, recyclability, and limitless number of possible structures (Singh and Savoy 2020), these new solvents have gained attention for cellulose processing, and have been used to produce a number of regenerated cellulose materials (Berga et al. 2020;Mezzetta et al. 2019a) and cellulose derivatives (Becherini et al. 2019;Ferreira et al. 2019).
This review encompasses the description of the basic concepts of ILs, their use to fabricate macro/ nano cellulose fibers, including the specifications for dissolving cellulose, the rheological features of cellulose-IL solutions in view of different manufacturing methods (i.e., wet-spinning, dry-jet-wet spinning, and electrospinning). Moreover, we review the development of new cellulose-based materials (e.g., composites or blend with other biopolymers), and we conclude with a perspective in the field. This comprehensive overview of the current knowledge on cellulose/IL systems and spinning technologies aims at encouraging further research towards the development of fully green products for the textile market.

Ionic liquids
ILs are organic salts characterized by a melting point lower than 100 °C. Asymmetrical organic cations in combination with either organic or inorganic anions generally destabilize the crystal lattice packing thus favoring the liquid state of the system in terms of enthalpy and entropy. The most intriguing peculiarity of these liquid salts is the possibility to modify their chemical and physical properties (e.g., viscosity, conductivity, hydrophilicity, hydrophobicity, polarity, hydrogen bond forming ability) by an appropriate selection of cation and anion, or by the introduction of specific functional groups in the chemical structure (Branco et al. 2011;Rabideau et al. 2020). Figure 2a shows some common IL cations and anions.
Within the last twenty years, ILs and the so-called room temperature ILs (RTILs), namely ILs which are liquid at room temperature, have gained attention for their potential application in several chemical fields including their use as solvents and catalysts for chemical syntheses (Clarke et al. 2018;Keaveney et al. 2017), separation technologies, or electrochemistry (Pereira et al. 2018). Noteworthy, ILs show unique properties such as high chemical and thermal stability (Maton et al. 2013;Mezzetta et al. 2019b), low vapor pressure, and no flammability (Singh and Savoy 2020;Welton 2018). Furthermore, the structural features of these ionic media provide unique chemical environments, which ultimately allow for the dissolution of several organic and inorganic species via specific interactions (Hayes et al. 2015).
For these reasons, ILs possess a superior dissolving capability even towards biopolymers, such as keratin (Idris et al. 2013) or cellulose that are difficult to dissolve in conventional solvents (Pinkert et al. 2009;Zhang et al. 2017a). Therefore, the interest for processing biopolymers with ILs has grown significantly in recent years. The high variability of ILs, due to the possibility of a combination of different cations and anions, leads to the development of new solvents endowed with specific properties that enable the dissolution of almost any specific substrate (Forsyth et al. 2004;Izgorodina et al. 2007).
However, the selection of a proper IL for biopolymer dissolution cannot be based only on the dissolution capability: other parameters like eco-toxicity and recyclability of the solvent, rheological properties of IL-biopolymer solutions, and characteristics of the regenerated biopolymer, must be considered in the process. In fact, ILs are not always innocent media towards dissolving biopolymers. For example, Nie and Zang (2017b) investigated how the structure of different ILs impacted keratin microstructure and the disulfide cross-linking network in regenerated keratin, while Shamshina and Berton (2020) reviewed the use of ILs in the depolymerization and deacetylation of chitin. The effect of ILs on the microstructure of cellulose after dissolution was analyzed in detail compared to other biopolymers. For instance, it is well known that the solubilization of cellulose in ILs leads to a variation of the degree of crystallinity, and this variation depends on the working conditions and ILs nature (Ling et al. 2017). Furthermore, reactions of solvated cellulose in ILs have been extensively reported and discussed in the literature: ILs have been used as solvents and catalysts for homogeneous functionalization of cellulose (Hanabusa et al. 2018) and for its transformation into low molecular weight molecules (Asim et al. 2019). Beyond these reactions, also undesired side reactions between cellulose and ILs have been observed. New chemical species can affect the properties of reprocessed cellulose material and the recyclability of ILs.
For example, for the first time Enber et al. (2008) described the reaction between C-2 of imidazoliumbased ILs and cellulose. Clough et al. (2015) also reported that imidazolium carboxylate ILs react with cellulose through the reactive C2 position of the imidazolium ring to generate a series of intermediates.
Liebert and Heinze considered three paths for side reactions of imidazolium salts including the fairly high reactivity of the anion as a nucleophile, the  (Pereira et al. 2018) abstraction of the C-2 proton of the 1,3-alkylimidazolium moiety, and ring-opening reactions (Liebert and Heinze 2008). They indicated that using C-2 alkyl substituted imidazolium ILs for the etherification of cellulose can decrease side reactions.
Other works (Gazit and Katz 2012;Michud et al. 2015a) reported the depolymerization of cellulose when imidazolium cations are used in combination with different anions. The Laborie groups (Abushammala et al. 2017;Zweckmair et al. 2015) analyzed the mechanism of the unwanted acetylation of cellulose by 1,3-dialkylimidazolium acetate ILs.
However, the in-depth study of many IL/cellulose systems allows for tuning different interactions of ILs with cellulose (Bodachivskyi et al. 2020;Clough et al. 2015). Therefore, the appropriate selection of processing conditions (e.g., type of cellulose, solvent, temperature, time, and even addition of co-solvent or additives) and the knowledge of IL characteristics permit the suppressing of side reactions while enabling the selective production of desirable cellulosederived materials.

Cellulose dissolution issues and role of ILs
The crystal structure of cellulose has a complex hydrogen bond (H-bond) network between the hydroxyl groups of glucose units of the same chain/ of different chains (Lindman et al. 2017). The intermolecular and intramolecular hydrogen bonds not only provide affordable strength and toughness of cellulose crystals and excellent mechanical properties, but also render cellulose insoluble in water and in most organic solvents, thus limiting its reactivity and processability for utilization. The issue of cellulose dissolution, to make this biopolymer usable in disparate processing and spinning operations, has always been on the agenda of scientific research in the last few years (Berga et al. 2020;Medronho and Lindman 2015). Before the introduction of ILs, alternative cellulose solvents and their limitations have been investigated.
In 1934, a combination of N-ethyl pyridinium chloride and nitrogen-containing bases was reported to dissolve cellulose (Graenacher 1934). In 1985, an improvement of cellulose solubility was observed by exploiting N, N-dimethylacetamide (DMAc)/ lithium chloride (LiCl) and also with N-methyl pyrrolidone (NMP)/LiCl (McCormick et al. 1985). However, solvent systems such as (DMAc)/LiCl, sodium hydroxide (NaOH)/urea, dimethyl sulfoxide (DMDO) (DMSO)/tetrabutylammonium fluoride (TBAF), have shown severe limitations including complex dissolving procedures, low solubility, hard solvent recovery processes, relevant energy costs, volatility, toxicity, gas pollution, and polymer degradation, thus limiting their large-scale use in industrial processes (Li et al. 2018). Due to the economic and environmental drawbacks of cellulose dissolution and processing, more efficient and environmentally friendly solvents have thus become a subject of intensive research.
In 2002, ILs have been explored for the processing of cellulose to replace conventional noxious solvents. They can be considered as the new generation of solvents for a more sustainable industrial development (Swatloski 2002). The dissolution of cellulose using ILs can construct a new platform for ''green'' cellulose usage and can also provide, a "green" possibility of nanocellulose preparation (Zhu et al. 2006). The main advantage of this procedure is that cellulose can be easily regenerated by the addition of a non-solvent (e.g., water). NMMO monohydrate-based Lyocell process is so far the benchmark spinning process. In fact, NMMO monohydrate has one major advantage over ILs, since a considerable amount of water can be left in the system during its recovery. The increased water sensitivity of ILs requires energy-intensive evaporation of water down to a low weight percentage and is a cost factor to be considered.
In addition to cellulose fiber production, IL-technology also provides new opportunities to construct composites and also allows the in situ chemical modification of cellulose during the spinning process (Hermanutz et al. 2019).
Heinze et al. (Kostag et al. 2018) presented a comprehensive review about the dissolution process of cellulose in ILs. Several research works have shown that cellulose solubility in ILs is strongly dependent on (i) process parameters like time required for dissolution, temperature, or heating method, (ii) cellulose parameters like degree of polymerization or crystallinity, and (iii) ILs parameters like, purity, water content or ILs structure (Schlufter et al. 2006;Swatloski 2002). The efficiency of the ILs in the dissolution process depends on the polarity and the hydrogenbonding ability between IL components and cellulose chains (Figueiredo et al. 2015). It is generally believed that H-bond formation between anions and the hydroxyl groups of cellulose is the main driving force for cellulose dissolution in ILs (Fig. 3b). Indeed, the high ionic strength of the ILs allows for disrupting the inter-and intramolecular hydrogen-bondingbased interactions present in pristine cellulose chains (Kostag et al. 2018;Vitz et al. 2009). Specifically, the intermolecular anhydro glucose units (AGUs) of cellulose are bonded by H-bonds between the equatorial OH of C3 and the oxygen of C6 of an adjacent chain. In this way, cellulose molecules are linked in a layer, and the hydrophobic interactions, due to the axial CH of AGU, hold together the layers forming the conformation of native cellulose (cellulose I) and of other allomorphs (cellulose II, IIII and IV, etc.) (El Seoud et al. 2020;Nishiyama et al. 2002). Physical dissolution of cellulose requires the disruption of the intramolecular H-bonds between the hydroxyl groups of the AGUs, as well as the hydrophobic interactions present between the layers.
Starting from the pioneering work of Swatloski et al. (2002) cellulose dissolution mechanism in ILs has been widely studied. Firstly, the role of the anion in the dissolution process has been analyzed: ILs with anions like nitrate (NO 3 ), triflate (F 3 CSO 3 ), ethyl sulfate (EtSO 4) , tetrafluoroborate (BF 4 ), hexafluorophosphate (PF 6 ), exhibit low cellulose solubility, while acetate, phosphate and formate anions have a higher ability to play as hydrogen bond acceptors: therefore, they are better choices for cellulose dissolution (Medronho et al. 2012;Swatloski 2002;Wang et al. 2012). However, the structure of the cation also affects the solubility process (Lu et al. 2014;Zhang et al. 2016). In fact, the cation can increase substantially the solubility by forming hydrogen bonds with hydroxyl groups and acetal oxygens of cellulose (Lu et al. 2014). Imidazolium, phosphonium, ammonium, or pyridinium cations favor cellulose dissolution: increasing the alkyl chain length in the (imidazolium) cation reduces cellulose solubility. Moreover, it has been shown that cations with even numbered alkyl side chains display higher cellulose solubility than those with odd numbers in the C2-C10 series, and this effect may partly be related to the IL viscosity (Vitz et al. 2009). In summary, several different structural features of the ion components of an IL, such as acidic H-atom and allyl groups, length of the alkyl chains and/or presence of functional groups, compete to determine the ease or the difficulty of cellulose dissolution in these media. Some general trends have been reported and structural effects of cellulose dissolution ability are known (for instance saturated alkyls and bulky groups in anion/cation have detrimental effects), while other aspects are still a matter of investigation (Xu et al. 2018a).
The chemical structure of the IL is not the only feature that should be evaluated for designing a good dissolution process giving that many parameters such as the viscosity of ILs and of the IL-cellulose solution, the IL water content, the heating mode (classic or microwave), and the thermal stability of ILs play also significant roles. (Lindman et al. 2010;Ruan et al. 2004aRuan et al. , 2004bZhu et al. 2006). For example, Pinker et al. (Pinkert et al. 2009) reported that dissolution times longer than 12 h do not lead to good results, and high temperatures cause the risk of partial degradation. In general, the working temperature depends on the degree of polymerization and on the cellulosic source. In fact, cellulose with a high degree of polymerization results in a very viscous solution in ILs and, by varying the temperature, it is possible to  (Ingildeev et al. 2013) adjust the viscosity of the solution (Druel et al. 2018;Zheng et al. 2019). In general, to increase the solubility percentage, impressive results have been obtained when microwave (MW) pulses of 3-5 s are applied instead of conventional thermal heating. MW heating is characterized by an internal heating process due to the direct absorption of energy which is responsible for the more effective breakage of the H-bonds present (Feng and Chen 2008). It is worth stressing that low-temperature processes have to be preferred since higher reaction temperature, as well as longer reaction times and strong agitation are harsh conditions for processing cellulose in ILs that, in turns, could ultimately change the structure of the biopolymer .
Nowadays, several ILs are known as cellulose solvents, but only a restricted number of them has been reported to date for the fabrication of cellulosic fibers (Table 1). These so-called first-generation spinning ILs typically comprise an imidazolium cation with chloride as the anion. As already mentioned above, the work of Swatloski et al. has opened new possibilities to process cellulose (Swatloski 2002). They reported that cellulose can be dissolved in 1-butyl-3-methylimidazolium ([Bmim])-based ILs such as 1-butyl-3-methylimidazolium chloride ([Bmim][Cl]) in rather high concentration (up to 15-20%) within a short time (1-12 h) and without any pretreatment and derivatization. Zhang et al. (2005) employed 1-allyl-3-methylimidazolium chloride ([Amim][Cl]) to produce solutions containing up to 5 w% of nanocellulose. The presence of chloride atoms in imidazolium-based ILs is highly effective in breaking the hydrogen-bonding network in cellulose, while the presence of water in ILs reduces the solubility (Swatloski et al. 2004(Swatloski et al. , 2002. However, some drawbacks such as the high melting point of imidazolium chloride and the corrosive character of halides toward metal processing equipment led to the exploration of alternative anions, such as acetate and dialkylphosphates. The use of 1-ethyl-3-methylimidazolium acetate [Emim][Ac] at room temperature showed some side reactions like cellulose acetylation, which limits its use for cellulose dissolution (Köhler et al. 2007).
Analyzing the data summarized in Table 1, one of the best ILs to dissolve cellulose is 1-butyl-3-methylimidazolium acetate ([Bmim]OAc), which showed 23 g/mol solubility at 40 °C. However, at the same temperature, changing the cationic structure to 1-methoxyethyl-3-methylimidazolium resulted in a significant decrease to 8 g/mol solubility (Lu et al. 2014). Other important values of cellulose solubility were found to be around 15 w% for [Amim]Cl at 80 °C that can be increased up to 20-25 wt.% with microwave heating (Kosan et al. 2008). Medronho et al. (2012) hypothesized that cellulose would be soluble in ILs and N-methylmorpholine-N-oxide because of their ability to weaken also the hydrophobic interactions. Some 1,3-dialkylimidazolium forms displayed substantial dissolution capacity of up to 22 w% (Fukaya et al. 2006).
Another class of ILs capable of dissolving cellulose is that of protic ILs (PILs). This class of ionic solvents is particularly attractive from both the synthetic and the cost perspectives. In fact, PILs are simply prepared by the addition of a Brønsted acid to a Brønsted base, thus reducing to the minimum the synthetic steps required, the use of solvents, and the workup procedure. Typically, superbases such as 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU), 1,5-diazabicyclo[4.3.0]non-5-ene (DBN), 7-methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene (mTBD) or 1,1,3,3-tetramethylguanidin (TMG), are employed in the preparation of PILs since their high basicity provides complete conversion even with weak carboxylic acids. PILs composed of a weak acid and a superbase with a low boiling point are called distillable ILs (DILs). In fact, by exploiting the acid-base equilibrium, the volatile precursors can be distilled thus making the ionic liquid distillable. King et al. reported the first examples of DILs composed by 1,1,3,3-tetramethylguanidine (TMG) with different carboxylic acids (formic, acetic, and propionic acids) and these systems were able to rapidly dissolve cellulose. The cellulose solubility depends on the alkyl chain length of the carboxylate anion while all tested PILs were recyclable by distillation with recoveries and purities higher than 99% (King et al. 2011). Based on these structures, cellulose solvating capability of structurally related DILs with different carboxylate anions and a range of bases and superbases of varying basicity has been recently investigated (Parviainen et al. 2013;Olga Kuzmina et al. 2017). The maximum amounts of cellulose dissolved in carboxylate DILs are reported in Table 1. Cellulose solubility does not seem to strictly correlate with the difference in acidity between acid and base (ΔpK a ). Indeed, several PILs exhibit disparate cellulose solubilities, despite very similar ΔpK a  values. Although all DILs with carboxylate anion are distillable with high purity, it is worth mentioning that TMG-and DBU-based DILs are more viscous than DBN-based DILs, which makes these latter systems of interest for rapid cellulose dissolution. The carboxylate anions ability to disrupt the hydrogen bond network of cellulose is also predominant for the dissolution of cellulose in carboxylate-based PILs. However, the hydrophobic alkyl chains would prevent interactions between carboxylate ions and hydroxyl groups of cellulose, thus decreasing cellulose solubility with increasing alkyl chain length of the carboxylate ion (Hideki Hanabusa 2019). For this reason, [DBNH]OAc was the first non-imidazoliumbased ionic liquid that was used for spinning of cellulose solutions demonstrating extraordinary properties (Michud et al. 2016b). Furthermore, the low cost of PILs, compared to traditional aprotic ILs, prompted their use in biomass deconstruction processes (Tu et al. 2020). An intriguing potential of ILs as solvents for cellulose is also their use as components of organic electrolyte solutions, intended as mixtures of an ionic liquid and a neutral polar co-solvent such as dimethyl sulfoxide (DMSO) or γ-valerolactone. This class of cellulose solvents is attracting increasing attention because of the rapid or instantaneous dissolution ability, the decreased viscosity, the enhanced thermal stability, and the possibility to finely-tune their physicochemical properties. Starting from the pioneering work of Rinaldi (2011), several organic electrolyte systems based on ILs and polar solvents for cellulose dissolution were developed (Clough 2017  1,3-dimethyl-2-imidazolidinone (DMI), DMSO, sulfolane and γ-valerolactone were able to dissolve 10% w/w of cellulose within seconds or few minutes. The co-solvent has been shown to improve the solubility of cellulose, even with ILs that in their pure form are not able to do so. In the form of organic electrolyte solutions, ILs such as tetra(n-butyl)ammonium acetate (Huang et al. 2016), tetra(n-butyl) ammonium fluoride, (Ciacco et al. 2003) tetraoctylphosphonium acetate, trioctyl(tetradecyl)phosphonium acetate, (Holding et al. 2017) and tri(n-octyl)methylphosphonium acetate (Holding et al. 2014) were able to solubilize up to 19% w/w of cellulose. A valuable example of organic electrolyte solution for cellulose solubilization was reported by King et al. (Holding et al. 2014 who analyzed different mixtures of acetate amphiphilic phosphonium ILs and DMSO in several ratios. One of the major advantages of these systems is that the hydrophobic IL can be easily recovered by phase separation at the end of the dissolution procedure when water was added. As reported, a wide portfolio of systems capable of dissolving, purifying, modify and spinning cellulose is currently available. Therefore, the choice of the best system has to be made on the basis of the starting cellulosic material and the characteristics of the material to obtain. Despite the advantages of IL-based solvents for the dissolution of cellulose, it is worth stressing that they have intrinsic drawbacks (Heinze et al. 2005). Toxicity of ILs is for instance one of the major concerns that must be addressed especially for biomedical applications in which cellulose-based materials may end up in the body. Even if the biomaterial is purified before implantation, there may still be IL effects in the material. It is important to stress that IL-based cellulose products will never reach to the market if IL impurities can affect the health of a patient. In the recent past, the topic of IL toxicity has gained much attention. The classification of the harmfulness of ILs was collected for different IL-types by Pham et al. (2010).
Owning to the demand for nontoxic ILs, several research groups have developed alternative ILs with the same favorable characteristics (i.e., low melting points, low viscosities) but without toxic components or degradable products. Quaternary ammonium, imidazolium and phosphonium cations (Kagimoto et al. 2006) have been combined with anions like acetate, tartrate, or amino acids. The resulting ILs are still characterized by a relatively low melting temperature and high solubilizing power for different chemicals (Anderson et al. 2007;Xue et al. 2006). Figure 2b shows the chemical structure of nontoxic anions. In the recent years, the trend of replacing petroleumderived constituent of ILs with natural or bio-based ions has emerged. In this regard, the components of ILs for cellulose treatment have also undergone variations in their structure aimed at the introduction of bio-based ions. In this scenario, Guazzelli et al. reported a series of novel ammonium, phosphonium and imidazolium ILs based on levulinic acid (LA) as the anion. Levulinic acid can be prepared, via an acidcatalyzed reaction, from cellulose and can be used for preparing cellulose-derived ILs, which in turn display a surprising high ability to dissolve their parent polysaccharide. In fact, the imidazolium ILs were able to dissolve a considerable amount of cellulose (up to 38 w%), while the hydrophobic ILs, used in electrolyte solutions, reached 12%wt for [N 8881 ]Lev:DMSO and 10 w% for [P 8881 ]Lev:DMSO (Mezzetta et al. 2019a). In a previous work, Guazzelli et al. also reported the preparation of protic levulinate ILs (Lev PILs) carried out by adding equimolar amount of levulinic acid to DBU or DBN, and tested them as cellulose dissolution and functionalization media. The solubilization performance of levulinate based ILs are summarized in Table 1 (Becherini et al. 2019).
As a conclusion of this section, it is important to stress that although ILs hold great promise as media for cellulose dissolution, specific criteria need to be met for further process development: in particular, the IL has to be easy to synthesize, recyclable at least at 99.5%, with the lowest possible toxicity, no vapor pressure, and high dissolution capability towards different pulp sources (Hermanutz et al. 2019).
Although the recyclability of ILs is promising, due to the current market scale and the relatively high cost of ILs, no industrial technology is yet available for IL recycling with the goal of reuse, and several challenges must be still addressed before IL pretreatment technology can become commercially viable (Abu-Eishah 2011). Most of the published works on IL recycle, rely upon extracting a solute from a mixture via suitable ILs, then recovering them for further reuse. The number of trial cycles in most cases was low (3 to 5 cycles) (Shamshina et al. 2021). One of the most important challenges is the affordable and scalable recovery and recycle of the IL itself (Sun et al. 2017). There are also some challenges when binary solvent systems containing IL and co-solvent are used, due to possible phase separation during recycling of the ternary system IL/co-solvent/antisolvent (Sun et al. 2017).

Spinning of cellulose with ILs: advantages and limitations
Various spinning techniques such as melt-or solution-spinning can be used to produce filaments, continuous fibers of indefinite length. Solution spinning methods can be categorized into dry-spinning, wetspinning and dry-jet-wet spinning. In any type of spinning method, a spinning dope is formed through melting or dissolving the polymer precursor that is then extruded through spinneret. Solidification of the dope can be obtained through cooling, solvent evaporation in a hot atmosphere or precipitation in a non-solvent. These techniques are referred to as melt-, dry-and wet-spinning, respectively (Stibal et al. 2000). High polymer chain alignment, which is key to high stiffness and strength, can be achieved by drawing the fiber immediately after the spinneret, or in a separate step, or by some combination of the two. Solution spinning techniques usually lead to greater mechanical performance by carefully controlling the amount of molecular entanglement (Clemons 2016).
Another widely reported method is electrospinning, in which a high voltage electrical field that is applied between the nozzle and a conductive collector leads to uniaxial elongation of the polymeric jet from a melt ink, solution, emulsion, or dispersion. The optimal spinning approach for a particular polymer is selected based on the polymer melting point, melt stability, or solubility in organic and/or inorganic solvents. The ability to form fibers of a particular polymer dope is often defined as spinnability. To evaluate the spinnability of a dope, several factors have to be considered, such as flow, rheology, melt flow index (for melt-spun polymers), crystallization, phase transition, solvent/solvent system behavior, and structure development (Lundahl et al. 2016).
The production of pure cellulose fibers is a challenging task since cellulose is scarcely soluble in conventional solvents due to notable inter-and/or intra-molecular hydrogen bonding (Quan et al. 2010).
In addition to its low solubility, cellulose is also difficult to be processed from the melt. Hence, processing of cellulose requires either chemical derivatization followed by regeneration or physical dissolution in non-derivatising solvent (e.g., N-Methylmorpholine-N-oxide (NMMO), Cuoxam, ILs) and consequent regeneration (Quan et al. 2010;Röder et al. 2009).

Solution-spinning
The history of man-made cellulose fibers (MMCF) starts from the discovery of cellulose nitrate by Karl-Friedrich Schönbein in 1846. The high flammability of nitrocellulose limited respective fibers for textile applications. Comte de Chardonnet was the founder of the MMCF industry in 1889. Even though the process was simple in principle, it faced some limitations including difficulties to scale up safely the production with a consequent limited economic potential.
In 1892, the foundation of the Viscose process changed the approach by involving the activation of cotton and wood cellulose in aqueous sodium hydroxide solution followed by reaction with CS 2 to form a cellulose xanthate (Cross et al. 1892). After dissolution in alkaline solution, the cellulose xanthate is spun into a sulfuric acid bath. In this method, in addition to other auxiliaries (e.g., carbon disulfide, sodium hydroxide, sulfuric acid, zinc sulfate), a considerable volume of fresh water is required (Hermanutz et al. 2019). To overcome the problems related to the extensive use of CS 2 , it has been developed the so called second cellulose processing that is based on the dissolution of cellulose in aqueous systems using solvation-mediators. For example, in cupro process cellulose fibers produce via a spinning process using a copper-based complexing agent such as tetraaminecopper dihydroxide (Burchard et al. 1994;Zhang et al. 2018). Another class of aqueous cellulose solvents is based on alkaline systems in which cellulose should be activated in a pretreatment step. However, alkaline solutions can handle only low-DP cellulose, which results in fiber with low strength.
The third type of cellulose dissolution is based on the discovery of NMMO monohydrate as a nonaqueous, non-derivatizing solvent for cellulose. In this technique that is known as the Lyocell process, NMMO monohydrate dissolves cellulose directly and spin dope can be dry-jet wet spun into an aqueous coagulation bath (Fink et al. 2001). Isopropyl gallate usually is used to stabilize the spinning dope to prevent side reactions. By spinning through an air-gap, high stretch ratios can be applied, which lead to the formation of long and thin crystallites align along the fiber axis. Therefore, there is little lateral interaction between the macrofibrils, which results in a high tendency to fibrillation in the wet state (Hermanutz et al. 2019). A pronounced lateral orientation leads, instead, to high mechanical performance of Lyocelltype fibers (Gindl et al. 2008). Despite the benefits of Lyocell process, such as minimum pulp losses and quantitative recycling of the solvent, NMMO monohydrate suffers from some intrinsic shortcomings resulting from the redox-active N-O moiety and the thermally labile cyclic ether structure. Therefore, from an environmental and economic point of view, the application of alternative direct cellulose solvents has gained interest in the scientific and industrial communities. Other direct solvent systems such as electrolyte solutions or phosphoric acids have been investigated but faced with some limitations including complex dissolving methods, cumbersome solvent recovery processes, and low solubility, which limit their large-scale use in industrial processes (Ahn et al. 2016;Rosenau et al. 2018).
As mentioned above, RTILs have emerged as desirable green solvents that can dissolve and process biopolymers such as silk (Gupta et al. 2007), wool (Xie et al. 2005a), chitin and chitosan (Wu et al. 2008;Xie et al. 2006), lignocelluloses (Kang et al. 2013), wood (Pu et al. 2007), and cellulose (Rahatekar et al. 2009b) with promising properties. They have been studied intensively within the latest 15 years, since Rogers and his co-workers rediscovered the ability of selected ILs to dissolve cellulose in high concentrations (Swatloski et al. 2004;Swatloski 2002). Fiber spinning of cellulose using ILs offers advantage of a simple, single step dissolution process cellulose solution without derivation, and without the addition of stabilizers, ensuring the design of both fibrillating and nonfibrillating fibers (Rahatekar et al. 2009b). In particular, these IL-based spinning dopes can be either processed by wet spinning or by dry-jet-wet spinning, allowing for the modification of fiber characteristics according to the envisaged application. Solubility of cellulose in ILs also facilitates the electrospinning process of this material to produce fibers with tunable properties (Isik et al. 2014  ) and [DBNH]OAc, have been used for cellulose spinning (Zhang et al. 2017a). In 2002, Swatloski et al. (Swatloski 2002) studied the possibility of producing fibers and films from cellulose-ILs solutions.

Dry-jet-wet spinning
The first attempts towards a technical conversion of the fiber processing were performed by Bentivoglio and co-workers (Bentivoglio et al. 2006;Laus et al. 2005), who reported the properties of fibers for textile applications.  (Zhang et al. 2005). Later, properties of cellulose fibers spun from ILs solutions were investigated by the BASF Company, the Institute for Textile Chemistry and Chemical Fibres (ITCF) and the Institute of Textile and Plastics Research (TITK) using a pilot manufacturing plant (Hermanutz et al. 2008). Wet and dry-jetwet spinning have been successfully exploited using [Bmim] as the IL. In order to avoid corrosion, cellulose decomposition, and to handle the IL with its fairly high melting point 70 °C, ([Emim]OAc) as noncorrosive ionic solvent was selected, and dry-jet-wet spinning process derived from the NMMO monohydrate process was developed and adapted to this IL solvent. Fibers achieved higher tenacities in comparison to conventional wet-spun fibers, which were comparable to Lyocell fibers.
In 2008, Kosan et al. produced cellulose fibers via a dry-jet-wet spinning process and compared 5 types of ILs with NMMO monohydrate, and found that depending on the type of solvent, cellulose exists in different solution states and the tensile strength of all fibers from the IL regeneration process was superior to the Lyceoll fiber (NMMO monohydrate process) (Kosan et al. 2008).
In a following study, they investigated the acetylation of cellulose in different ILs without using catalyst and the subsequent dry/wet spinning process. After the dissolution of cellulose in the IL (first step), and the homogeneous modification of cellulose to cellulose acetate (second step), cellulose acetate fibers with controlled degree of substitution (DS) values and properties were obtained (Kosan et al. 2010). Afterwards, the rheological behavior of the cellulose/ ([Bmim]Cl) solution was investigated by Cai et al. (2010), and the fibers were spun with a dry-jet-wetspinning process. The obtained fibers had crystalline polymorph of Type-II similar to Lyocell fibers. Orientation, crystallinity, and consequently the mechanical properties of the fibers, were improved by increasing the draw ratio. To prepare the cellulose/([Bmim] Cl) spinning dope with fewer particles, lower apparent viscosity, and higher uniformity, they developed a two-step dissolving process, in which cellulose was first swelled to its maximum volume in aqueous [Bmim]Cl solution, and then dissolved by stirring under vacuum to remove excessive water. By using this new dissolving process, spinnability and mechanical properties of regenerated cellulose fibers improved when compared to the direct dissolving process (Cai et al. 2012). Jiang et al. (2012Jiang et al. ( , 2011 produced regenerated cellulose fibers from bagasse and wood, and obtained fibers with the tensile strength of 630 MPa via increasing the spinning speed. The regenerated bagasse fibers had higher crystallinity and tenacity than the regenerated wood fibers. Hong et al. (2013) prepared cellulose fibers using cellulose/ [Emim]OAc: dimethylformamide (DMF) solution under dry-jet-wet spinning conditions. The presence of DMF decreased the solution viscosity and improved spinnability and the fiber surface, but it led to a reduced crystallinity and tensile strength of the fibers. Ingildeev et al. (2013)  OAc as recyclable solvents for dissolving raw cellulose in order to spin micro-and nano-scale regenerated cellulose fibers. The comparison of the properties of the spun fibers in terms of tensile strength, crystallinity and thermal decomposition, demonstrated that [Emim]OAc is a better candidate for dissolving cellulose because it requires lower dissolving and spinning temperatures than those of [Bmim]Cl, and needs less energy for the fiber formation. Besides, [Emim]OAc residuals are not toxic and safe for both consumers and healthcare end-users. In the dry-wet spinning process, many parameters, such as influence of pulp source, degree of polymerization of cellulose, mass distribution, concentration of the spinning dope, type of solvent, drawing ratio in the air gap, spinneret diameter, extrusion velocity, draw ratio, and coagulation bath temperature impact the mechanical properties of fibers (Michud et al. 2016a;Wendler et al. 2009a, b).
Sixta et al. developed a novel regenerated cellulose fiber process of the Lyocell type, denoted Ioncell via using of powerful direct cellulose solvent, [DBNH] OAc in which airgap spinning can be conducted at higher cellulose concentration in the dope, and lower temperature is used during dissolution and spinning (Sixta et al. 2015). Cellulose is less degraded due to the generally mild process conditions, which result in both high fiber yield and strength properties. The effect of different cellulose concentrations and draw ratios on the fiber properties have been investigated in their work and the highest tenacity was achieved by spinning from 15 wt% to 17 wt% cellulose solutions. A very high initial modulus of up to 34 GPa made the Ioncell fibers very interesting for technical applications. The effect of dope concentration and the stretching rate influence in Ioncell process on the fiber characteristics is also confirmed by Sun et al. (2015b).
In a series of studies of cellulose solution spinning with [DBNH]OAc, Michud et al. (2015b) demonstrated that the distribution of cellulose chains, the presence of a specific rheological matrix of zero-shear viscosity, and the dynamic modulus of the spinning dope have a considerable effect on the spinnability of cellulose/IL solution. They also indicated that the MMD of the cellulose chains contributed to the tensile strength. High-molecular weight cellulose chains combined with a low-fraction of the short-cellulose chain (DP < 100) are desirable for obtaining high strength cellulosic fibers. By using cotton linters, spruce sulfite pulp (68.7:31.3%) with an intrinsic viscosity of 433 ml/g, cellulose fibers with the tensile strength of 70 cN tex −1 approximately 1 GPa, according to the conversion proposed by Maenner et al. (2011) assuming fibers with a perfect round cross-section and a density of about 1.5 g/cm 3 was obtained.
Hauru et al. (2014) found that the increase of the temperature of the coagulation bath resulted in a decrease of the fiber tenacity. Olsson et al. (2014) demonstrated that application of N-methylimidazole (MIM) as a co-solvent with [Emim]OAc and [Bmim]Cl, provided better solubility of microcrystalline cellulose (MCC), higher dissolution rate and lower solution viscosity. The stable solution successfully converted to regenerated fibers with high crystallinity and good mechanical properties via both dry-jet-wet spinning and traditional wet spinning. Low molecular weight MCC, which is often used for low mechanical performance applications, was converted into highly aligned and stiff regenerated cellulose fibers (Young's modulus ~ 22 GPa) using [Emim][(EtO) 2 PO 2 ] as ionic solvent, optimizing the solution concentration (18w%) and applying a high fiber extrusion/winding ratio during the dryjet-wet spinning process ). By using DMSO as a co-solvent with [Emim][(EtO) 2 PO 2 ], and increasing the concentration of cellulose (20.8 w% and 23.6 w%), considerable alignment of cellulose chains along the fiber axis and, consequently, cellulose fibers with exceptional mechanical properties (Young's modulus ~ 41 GPa) were produced (Zhu et al. 2018). Ma et al. produced cellulose fibers with high tensile strength via dry-jet-wet spinning of cellulosic waste such as paper and cardboard using [DBNH]OAc) as ionic solvent (Ma et al. 2016). Most of the studies briefly summarized above are based on imidazolium halide or carboxylate ILs that produced filaments with diameters of about 100 μm. Depending on the spinning method, there are specific chemical and physical requirements to extrude continuous filaments on a commercial scale. Specifically, ILs should be thermally stable to keep the solute stable at the required processing temperatures since the extreme degradation of the IL and biopolymer may be an issue for solvent recovery and recycling. Therefore halide-based ILs has a substantial limitation for scaling-up the technology (Kosmulski et al. 2004). In contrast, carboxylate-based ILs could overcome this problem to some extent (Michud et al. 2015a). Besides the thermal and chemical stability of ILs, distinct viscoelastic properties of IL-polymer solutions have to be suitable for an industrially applicable spinning process. A key particularity of the dry-jet-wet spinning method is the draw of the fluid filament in the air gap that leads cellulose chains to align along the fiber axis and forms filaments with lower diameters and high mechanical properties (typical for Lyocelltype fibers). The filament breaks in the air gap if it is too thin at its exit point, so that the draw-ability of an initially thick filament is important to achieve thin and strong fibers. The archetypical IL, [Emim] [Ac], is a desirable cellulose solvent due to its low viscosity but, since the solution lacks the required elasticity, filaments cannot be extensively stretched.
Recently, a wet-type solution blow spinning mechanism with a water-mist coagulation chamber has been developed to produce fine regenerated cellulose fibers from the non-volatile IL solvent ([Emim][Et 2 PO 4 ]) (Fig. 4a). Within the optimum spinning condition, a non-woven fabric from fine fibers with an average diameter of 0.98 ± 0.62 μm was fabricated directly using a multi-nozzle spinneret (Fig. 4b). Drag force of the hot air and rapid coagulation in the water mist led to well-defined molecular orientation and high crystallinity (up to 67.6%) (Zhang et al. 2019a). Table 2 shows mechanical behavior of cellulose fibers produced with dry-jet-wet spinning methods from different cellulose sources. According to this table, the highest tensile strengths were 850 MPa related to the cellulose fibers using Spr.NH4-S pulp source, with DPw = 722, dissolved in [Bmim]Cl, produced by a dry-jet-wet spinning technique collected in the water bath at 85 °C and 852 MPa related to the cellulose fibers using Eucalyptus pulp (Eu-556) source with DP = 556, dissolved in [Bmim] OAc, produced by a dry-jet-wet spinning technique collected in the water bath.

Wet spinning
To fabricate cellulose fibers via wet-spinning process, the viscosity of cellulose solutions has to be decreased through an increasing spinning temperature (Kim and Jang 2013), reducing dope concentration (Ingildeev et al. 2013), and using co-solvents . Smaller spin capillaries with a smaller diameter can be used in the wet spinning of IL-biopolymer solutions; subsequent draw forces are considerably smaller, which prevent filament breaks. However, the fibers fabricated with this process have low mechanical properties since polymer alignment is mostly confined to shear-induced orientation in the spin capillary, and stretching of the filament in the spin bath is also only possible within limits. Therefore, since dry-jet-wet spinning is the more promising method for processing of IL-biopolymer solutions, suitable viscoelastic properties of the solution are a mandatory requirement (Rosenau et al. 2018 They reported that the IL anion significantly affects the coagulation kinetics owning to its association with cellulose and deduced that imidazolium-based ILs containing halides or carboxylates are efficient cellulose solvents and have been adopted for cellulose spinning. However, depending on the substituent on the imidazolium ring and the chemical nature of the ionic liquid anion, they can degrade cellulose at high temperatures (> 90 °C) (Ebner et al. 2008). Sun et al. (2015a) introduced a new kind of environment-friendly wetspun cellulose fibers by using a new cellulose solvent, TBAA/DMSO. The cellulose/TBAA/DMSO solution is a typical shear-thinning fluid. Cellulose fibers with a smooth surface and compact structure with strength as high as 375 MPa were obtained. This numerical value is similar to that of viscose fibers but lower than that of dry-jet-wet spinning fibers. Ingildeev et al. (2013), observed that the fibrillation of fibers that occurred during the dry-jet-wet spinning process was avoidable in the wet -spinning process of cellulose using [Emim] OAc as ionic solvent (Fig. 5). Wet-spinning process of four cellulosic materials (MCC, cotton linter pulp, bamboo pulp, and bleached softwood sulphite dissolving pulp) and six non-derivative solvents was investigated by Chen et al. (2015a) to find the combined effects of materials and solvents on the preparation, and on the structural and mechanical properties of regenerated cellulose fibers. The results showed that the dissolving   Zhu et al. (2018) time was affected by the raw materials' properties (e.g., the molecular weight), but raw materials and solvents had no significant influence on the crystallinity and elongation at break of the fibers. The tensile strength of the fibers was directly dependent on the molecular weight of the raw materials, and varied with the type of solvents. The influence of degree of polymerization (DP) on the properties of spin dopes and wet-spun cellulose fibers from dopes of mixed cellulose sources has been investigated. A nonlinear relationship between DP and fiber features was observed and fibers composed of polymers with the highest DP showed the highest mechanical properties (Olsson and Westman 2013).
Regarding the several controllable spinning parameters, Hermanutz et al. (2013) wet-spun cellulose filaments with a fineness down to 0.2 dtex. Cellulosic fibers were directly spun from IL to fibers below 0.5 dtex. The high surface area is a main advantage of super-microfibers smaller than 5 μm in diameter, in comparison to standard microfibers produced in the 5-9 μm range. In recent work, wet spinning was used to produce cellulose fibers from cellulose/(IL)/co-solvent solutions.
[Emim]OAc, DMF, DMSO, and water with various compositions were used as co-solvents. The solutions were stable and converted to regenerated fibers with desirable properties via the conventional wet-spinning process. The presence of co-solvent led to increase of dissolution rate, reduction of the complex viscosity and increase of fibers crystallinity as a result of interaction between cellulose chains. Additionally, the plasticization effect of the co-solvent led to the increase of the mobility of the cellulose chain and a slight increase in tensile strain ( Fig. 5) (Lee et al. 2019). Luo et al. (2008) proposed a technique to produce regenerated fibers from cellulose dissolved in [Emim] OAc solvent and extruded by the melt blowing process with the goal of fabricating bonded non-woven webs. Table 3 shows the mechanical behavior of cellulose fibers produced with wet-spinning methods from different cellulose sources.

Dry-jet-wet spinning
A comprehensive understanding on the recrystallization of cellulose in ILs is of a paramount importance towards the regeneration process for fibers, films and nonwovens ). Actually, one of the main challenges for developing cellulosic materials from ILs is the understanding of crystallization, which affects the physical and chemical stability, and mechanical strength of the cellulose (Isogai et al. 2011;Wang et al. 2007). Several studies have reported quite low crystallinity of cellulose regenerated from ILs that may influence mechanical properties (Ahn et al. 2016). Native cellulose generally exhibits a polymorph structure of Type-I cellulose with the highest degree of intermolecular and intramolecular hydrogen bonding, while the crystalline polymorph of Type-II occurs when cellulose is processed with an IL (Salem 2018). The fast coagulation and regeneration of cellulose from the ionic solution might be an issue for the re-crystallization of cellulose chains. Indeed, when cellulose has been solubilized and regenerated, the transformation of cellulose type-I into type-II remains an irreversible process. This trend indicates that, during the dissolution process, IL molecules penetrate into the gap between hydrogen-bonded sheets in cellulose I and lead to a slight expansion of the lattice. Simultaneously, intermolecular hydrogen bonds are disturbed such that the long-range order within each sheet decreases (Cheng et al. 2012;Freire et al. 2011) (Fig. 6).
The addition of other microparticles or secondary (bio-) polymers, such as multi-walled carbon nanotubes (MWCNTs) (Rahatekar et al. 2009a;Zhang et al. 2007 (Song et al. 2013), silver particles and charcoal (Wendler et al. 2009a(Wendler et al. , 2009b  , has been also considered. Halloysite nanotubes (HNTs) (Luo et al. 2014) and nanolignin with cellulose solution using IL prior to the spinning process allow exploring the preparation of functional fibers with a specific physical, mechanical or biological properties. ILs are also ideal solvents since they can be used for the preparation of cellulose-polymer blends. In most cases, a small share of particles can also have a positive influence on the fiber strength until a certain threshold: once this limit is overcome, the tensile strength deteriorates with further addition of solids.
It is well recognized that the spinning process and fiber properties are strongly dependent on the rheological behavior of the applied cellulose/IL based solution. The shear rheological characterization   (Cheng et al. 2012) and solution viscometry are essential for determining polymer solution properties to design processing strategies. Thus, the understanding of the concentration-dependent shear and extensional rheology of cellulose dissolved in ILs as well as the dynamics and thermodynamics of cellulose chains dispersed in ILs, are necessary steps toward realizing the potential of ILs as processing aids in fiber spinning (Haward et al. 2012;Song et al. 2010). Early studies on the macromolecular nature of cellulose and cellulose derivatives, as well in ILs, have established many of the fundamental concepts regarding the relationships between solution viscosity, polymer molecular weight, and polymer-solvent interactions (Haward et al. 2012;Klemm et al. 2005;Song et al. 2011Song et al. , 2010Zugenmaier 2009). However, for cellulose/ILs composites and blends, the situation is quite different. The presence of nanoparticles, CNT, polymers, or other additives strongly alters the rheology and viscoelastic behavior of the solution system. Table 4 shows fiber properties from different composite cellulose fibers produced with dry-jet-wet spinning method and from different cellulose sources. Carbon nanotubes (CNTs) have been widely investigated owning to their excellent physicochemical and mechanical properties, and have an excellent potential as electrically conducting inclusions in textiles due to their great electrical conductivity and high aspect ratio (Xie et al. 2005b). They offer several advantages for polymeric composites, such as versatility as reinforcement in both thermoplastic and thermoset areas, extremely high tensile strength (150-180 GPa) and Young's modulus (640 GPa to 1 TPa), and their compatibility with other chemical compounds (Baur and Silverman 2007). Reinforcements with CNTs not only improve mechanical and thermal properties, but also provide additional functional properties. Preliminary studies have demonstrated the effect of multi-walled carbon nanotube (MWCNs) on thermal and mechanical properties of wet-spun cellulose fibers (Rahatekar et al. 2009b;Zhang et al. 2007). For the preparation of a polymer/CNT solution, a uniform CNT dispersion or a CNT solubilization in solvents is still challenging to achieve since CNTs have low surface energy, tend to form agglomerates, and are amphiphobic (repel common polar and nonpolar solvents) (Xie et al. 2005b). , Zhange et al. (2007 used AmimCl to fabricate regenerated cellulose fibers reinforced with different concentration of MWCNs via dry-jet-wet-spinning process. In order to determine the degree of MWCNT dispersion in the AmimCl, they considered the rheological properties of MWCNT/AmimCl mixtures (within 2-8 w% of MWCNTs in AmimCl). In this study, the critical MWCNT concentration was between 2 w% (liquidlike) and 4 w% (gel-like).
Smooth round surfaces were obtained for both cellulose fibers and cellulose/MWCNT composite fibers (Fig. 7a). At 4 w%, aligned MWCNs were well-dispersed within the cellulose matrix (Fig. 7a iii ). Higher CNT loadings resulted in aggregation of CNTs. The regenerated-cellulose/MWCNT composite fiber containing 4 w% MWCNTs exhibited improvement in mechanical properties.
MWCNs have been also successfully blended with cellulose using ethyl methylimidazolium acetate [Emim]OAc prior to the dry-jet-wet-spinning process. Rheological characterization of cellulose/ [Emim]OAc blends showed pseudoplastic shear thinning behavior. The 0.01, 0.03, 0.05, 0.07, and 0.1 MWCNT mass fraction solutions used for fiber spinning also exhibited a strong shear thinning behavior. Cellulose orientation and crystal size subsequently tensile strength and strain to failure of the fibers were significantly higher in the composite than in the control cellulose fiber while Young's Moduli essentially remained unchanged. A relative improvement (30%) in the tensile strength of MWNT/cellulose composite fibers was obtained by adding up to 0.07 mass fractions MWNT. Moreover, the composite fibers exhibited lower thermal shrinkage than the control cellulose fibers (Rahatekar et al. 2009a;Rahatekar et al. 2009b). Besides, Zhu et al. (2014) improved the dispersion of carbon nanotubes in [Emim]OAc and in cellulose solution dope by non-covalently surface modification of CNTs using carboxymethyl cellulose (CMC) (Fig. 7b). The influence of fiber extrusion rate and fiber winding speed on the degree of alignment of the electrical conductivity of the cellulose/carbon nanotube composite fibers was investigated.
Sun et al. prepared functionalized cellulosic fibers by using magnetite particles and 1-ethyl-3-methylimidazolium chloride as the ionic solvent (Sun et al. 2008). The fiber texture was affected by cellulose concentration, molecular weight in the spinning solution and magnetite concentration. The enhanced degree of polymerization (DP) and/or cellulose concentration improved mechanical properties of the fibers while the presence of magnetite particles weakens the overall mechanical properties. In a second work, (Maxim et al. 2012) the authors prepared nanomagnetite (NM)-loaded cellulose fibers via dry-jet-wet spinning using ([Emim]OAc) as an ionic solvent. The presence of 0.75% (mass ratio) nanomagnetite in the cellulose matrix significantly improved the mechanical properties of the fibers, while the higher amount of NM, led  Coscia et al. (2018) to a reduction of mechanical properties as a result of large agglomerates that create defects within fibers. The authors also incorporated TiO 2 microparticles inside the fibers to improve the antibacterial and photocatalytic properties of cellulose fibers using previous procedure. Results revealed that the presence of particles (5 w%) did not have a considerable effect on mechanical properties of fibers and particles have the tendency to outcrop the surface of the fibers that provided a large active surface area (Maxim et al. 2010). Song et al. (2013) used [Amim] Cl as a good solvent for cellulose and well dispersant for nano-SiO 2 to produce bio-nanocomposite fiber via dry-jet-wet spinning method. Generally, the presence of nanoparticles drastically alters the viscoelastic properties of the solution. In this study, from the oscillatory shear measurements for the microcrystalline cellulose (MCC)/nano-SiO 2 /AMIMCl solutions (with different content of nano-SiO 2 in a range of 0-12 w%), it was found that the storage moduli (G′) and viscosity of the solution enhanced with the increase of nano-SiO 2 content, and the gelatin network occurred above 10 w% nano-SiO 2 . Moreover, the shear viscosity of the solutions with nano-SiO 2 was lower than that of cellulose/IL solutions under high shear rates. At 8 w% well-dispersed particles were observed (Fig. 7c) and tensile strength of the nanocomposite fibers had the highest values. The regenerated cellulose and nanocomposite fibers were the typical cellulose II crystalline form, which was different from the native cellulose with the dominated polymorph of Type I. The nanocomposites exhibited higher thermal stability by increasing the amount of nano-SiO 2 .
Recently, Coscia et al. produced bio-renewable regenerated curcumin/cellulose composites fibers via dry-jet-wet-spinning method using [Emim][Et 2 PO 4 ] as the IL. Curcumin was found to be uniformly dispersed in cellulose fibers and led to formation of yellow fibers (Fig. 7d) (Coscia et al. 2018). The presence of curcumin improved mechanical properties of fibers. Such strong cellulose fiber with a pharmacologically potent drug curcumin could be applied for medicinal, cosmetic and food packaging applications.

Wet spinning
More recently, Liu and coworkers used an ecofriendly wet-spinning method (Fig. 8) to produce  (Song et al. 2013), d d i Macroscopic and d ii microscopic presentation of composite fibres. Cellulose with a concentration of 5% curcumin (Coscia et al. 2018) conductive MWCNTs-graphene sheets (rGOs)-cellulose fiber with a mass ratio of 2:3:1 in which 1-ethyl-3-methylimidazolium diethyl phosphate [Emim] [Et 2 PO 4 ] was used as both green solvent and dispersant (Liu et al. 2019). Results showed that the dispersion was improved as a result of the synergy effect of CNT and rGO in comparison to each individual component. The obtained fibers showed electrical conductivity of 1195 S/m, the specific capacitance of 597 mF/cm 2 , and a specific surface area of 91 m 2 /g.
Härdelin and Hagström dispersed carbon black (CB) and graphene nanoplatelets (GNP) in an IL ([Emim]OAc) based cellulose solution using shear mixing and produced carbon filler-loaded cellulose fibers using the wet-spinning method (Härdelin and Hagström 2015). The presence of CB and GNP particles in the spin dope led to the formation of micropores in the fiber. Low adhesion between cellulose and filler particles in combination with the developed microporosity led to the reduction of fiber tenacity.
To improve the thermal stability and tensile strength of the MCC fibers, Luo et al. (2014) incorporated halloysite nanotubes (HNTs), a new type of clay, inside the fiber using [Amim] Cl as ionic liquid solvents. The results indicated that the addition of HNTs not only modified thermal and mechanical properties but also significantly improved the moisture barrier properties of the regenerated MCC fibers. Table 5 shows fiber properties from different composite cellulose fibers produced with   Luo et al. (2014) wet spinning method and from different cellulose sources. The dependence of dynamic storage modulus (G ′ ), loss modulus (G ′′ ) and complex viscosity ( | * | ) for the 9 w% MCC/AMIMCl/HNTs dispersions with different content of HNTs measured. For the pure MCC/AMIMCl solutions, G ′ was always smaller than G ′′ and showed a typical liquid-like behavior. Rheological measurements showed that the dispersions had stronger shear thinning behavior and the dispersions displayed stronger birefringence with increasing HNT content.

Solution-spinning of cellulose/polymer blend fibers
Blend fibers consisting of man-made polymeric materials and natural and renewable biopolymers such as polysaccharides are well established in a multitude of applications such as textile markets. However, the physicochemical properties of natural polysaccharides like cellulose limit their processability. In this case, IL solutions may open a new window for the blend fiber production by substituting hazardous solvents for cellulose processing (Tavanaie 2013). Since ILs are able to dissolve a wide range of polymers, the production of cellulose-polymer blend fibers has received a lot of attention. However, the formation of a homogeneous solution of different polymers does not necessarily result in the formation of a homogeneous blend fiber phase separation can occur upon coagulation if polymers are not compatible. Generally, natural polymers tend to have a strong affinity to cellulose.

Dry-jet-wet spinning
In two extensive studies, 15 different polysaccharides were used to investigate their miscibility and processability with cellulose in solutions using [Emim]OAc (Wendler et al. 2010(Wendler et al. , 2011. The rheological behavior of the solutions was considered to investigate the effect of polysaccharide addition compared to pure cellulose solution. The results indicated that the blend solutions (especially, xanthan, gum tragacanth and LBG) exhibited higher viscosities and elasticity than the pure counterparts.
Polysaccharides with a structure similar to cellulose, e.g., xylan, were miscible, while high-molar and side chains containing polysaccharides such as xanthan gum formed co-continuous morphologies. Blend fibers produced with dry-jet-wet spinning represented lower physical properties compared to the unmodified fiber.
Cellulose/chitosan blends also show promising systems for creating new polymeric materials with improved properties. The reactivity of chitosan is more versatile than cellulose due to the presence of NH 2 groups (Dutta et al. 2004). Blend cellulose/chitosan fibers produced by dry-jet-wet spinning method with higher tensile strength in comparison to regenerated cellulose fibers have been reported using the mixture of glycine hydrochloride and [B 4 mim]Cl (Ma et al. 2012).
Lehmann and co-workers have demonstrated that cellulose can be co-processed with lignin added to the cellulose solution (Lehmann et al. 2013(Lehmann et al. , 2012. Some studies have used dry-jet-wet spinning to produce lignocellulosic fibers (Ma et al. 2015;Sun et al. 2011). Ma et al. (2015) produced high performance regenerated cellulosic fibers using recycled and low refined lignocellulosic materials using [DBNH]OAc as the IL (Fig. 9 a, a i ).
The relationship between the chemical composition/structure of the raw materials, hemicelluloses and two different types of lignin (isolated pure lignin and residue lignin in the native form), the viscoelastic properties of spinning dope, spinnability, fiber tensile properties and the morphology of the spun fibers have been investigated. The rheology measurement of the dopes indicated that the increasing of the Fig. 9 SEM images of cross section of composite fibers with a, 0%, ai 30% lignin (Ma et al. 2015) lignin content decreased the zero shear viscosity and dynamic moduli. To compensate for the loss of the zero shear viscosity, the solutions were spun at lower temperatures. Dissolution and spinning of lignin and cellulose blends with ratios as high as 1:1 can be achieved. Recycled lignocellulosic, such as fine paper, cardboard, and newsprint were also assayed for their spinnability through the Ioncell process in [DBNH]OAc. The dope prepared from recycled fine paper showed great spinnability.
Blending of cellulose with synthetic polymers using ILs is more complicated since hydrophilic areas in the polymer should facilitate miscibility (Ingildeev et al. 2012). Both formation of a homogenous copolymer matrix and phase separation upon coagulation of a Polyacrylonitrile (PAN)/cellulose IL solution have been reported (Ingildeev et al. 2012;Zhang et al. 2019b). Fibrillated regenerated cellulose fibers have been developed via the immiscible blending of PAN and cellulose in [Bmim]Cl (Fig. 10). Since fiber spinning greatly depended on rheological properties of spinning dope, the shear viscosity ( ) as a function of the shear rate was measured. The viscosity totally decreased with increasing shear rate, which indicated non-Newtonian flow and a typical highly viscous liquid. At low shear rates (below 5 s −1 ) the η of Cellulose/PAN blend solutions was larger than that of the Neat Cellulose. At higher shear rates (above 10 s −1 ), due to shear-thinning, a decrease of η was observed. For dry-jet wet spinning of fibers, the spinning dopes prepared with the fixed cellulose concentration of 10 w% and the weight ratio of Cell/PAN 100/10 and 100/20. DMSO was used to remove the PAN phase and mechanical fibrillation treatment was applied to the fibers into microfibrillated cellulose fibers. The immiscible polymer blending approach shows good potential for the production of fibrillated cellulose with controllable size via a simple and energy-saving method (Zhang et al. 2019b).
Cellulose/aromatic polysulfonamide (PSA) blended fibers were successfully produced using dry-jet wet spinning technology and [Bmim]Cl as the ionic solvent in order to improve flame-retardant, hydrophilic and mechanical properties. Results demonstrated a strong interaction between cellulose and PSA. The hydrophilic and mechanical properties of blended fibers was enhanced with increasing the content of cellulose (Wu et al. 2017). Mundsinger et al. (2015) prepared wet-spun cellulose fibers, containing up to 25 w% chitin using [Emim] OPr as a solvent. The rheology of the spinning dopes was investigated for different biopolymer ratios. Chitin/cellulose solutions with relatively low amount of cellulose exhibited very low zero shear viscosities compared to pure cellulose dopes. Decreasing the chitin to cellulose ratio (the total biopolymer concentration set at 8 w%) caused an increase in the zero Fig. 10 Schematic illustration of the preparation of cellulose microfibrils (Zhang et al. 2019b) shear viscosity of the mixture. A dope containing 6 w% of cellulose and 2 w% of chitin in [Emim]OPr displayed rheological properties that were sufficient for multifilament production. Wet-spun multifilament fibers were successfully obtained (Fig. 11a, a i ). Silva et al. (2016b) developed composite fibers of cellulose and duck feathers (Fig. 11b, c), using [Amim]OAc as common solvent with improved mechanical properties (+ 63.7% of the tensile strain) over regenerated cellulose fibers (RCF).

Wet-spinning
Other blend fibers such as cellulose/polyacrylonitrile, cellulose/polyamide (Ingildeev et al. 2012) and cellulose/polycaprolactone (Xiong et al. 2012) have been easily produced through concurrent dissolution of cellulose and synthetic polymer and subsequent wet spinning. Mutual miscibility of the two components is the most important factor which affects the mechanical properties of blend fibers. It is worth mentioning that even these promising first results; the synthesis of cellulose blends via IL solutions is still facing some challenges. Chemical derivatization and composites and blends formation of polysaccharides is limited by the low solubility and the low thermal stability of these materials. The presence of ILs with sufficient solubility of cellulose opens new windows for its functionalization and processing and can basically change the current situation. However, the advantages offered by IL for the synthesis of cellulose-based composites and blends have only been partially exploited to date (Pereira et al. 2018).

Electrospinning of cellulose with ionic solvents
Cellulose nanostructures have recently gained increased attention and found advanced applications in various fields. Nanocellulose merges the inherent features of cellulose and specific characteristics of nanoscale materials. Given that cellulose is one of the oldest polymers used in manufacture of fibers, it has been taken into consideration and proposed for production of nanofibers. Regenerated cellulose ultrafine fibers in the nanometer range due to special morphology and geometrical dimensions, possess improved properties different from conventional micro fibers, interesting for industrial applications (Bazbouz et al. 2019;Otsuka et al. 2017;Zhang et al. 2019c). Electrospinning is a simple and effective process to produce the polymeric nanofibrous materials for a wide range of applications. This method works based on the drawing of viscoelastic solution or melt under a strong electrostatic field (Foong et al. 2020;Maleki et al. 2020Maleki et al. , 2018Mokhena and John 2019;Udangawa et al. 2019). Fiber deposition using different collectors and by manipulating the electrical field can result in various structures in the form of randomly oriented webs or aligned bundles and yarns. Moreover, electrospinning allows modulating the characteristics and functionalities of nanofibrous structures by controlling the fiber features (morphology, diameter, crystallinity, porosity, etc.) by tuning solution properties and adjusting the process variables (Foong et al. 2020;Maleki et al. 2017;Zavgorodnya et al. 2017). The nanofibrous structures composed of electrospun cellulose fibers generally exhibit several excellent characteristics, likely very large surface area over volume ratio, high porosity with a very small pore size, mechanical reinforcement, and enhanced surface reactivity, which make them appropriate candidates for diverse technical, industrial, and biomedical applications such as functional textiles, filtration membranes, tissue engineering scaffolds, wound healing, drug delivery, etc. (Ahn et al. 2012a, b;Bazbouz et al. 2019;de Campos et al. 2019;Devarayan et al. 2013;Freire et al. 2011;Kang et al. 2013;Liu et al. 2017;Mokhena and John 2019;Nechyporchuk et al. 2016;Norrrahim et al. 2018;Otsuka et al. 2017;Zhang et al. 2019c;Zheng et al. 2014). In contrast to the advantages, due to the poor solubility of cellulose in volatile solvents, the electrospinning of cellulose is chalenging. The strong inter-and intra-molecular interactions of hydrogen bonding and rigid backbone structure of cellulose limit its dissolution in common solvents suitable for electrospinning. Thus, electrospinning of cellulose is challenging and specific procedures need to be considered for the fabrication cellulosic nanofibers using this method (Abdul Khalil et al. 2015b;Frey 2008;Härdelin et al. 2012;Hsieh 2018;Kargarzadeh et al. 2018;Le Corre et al. 2014;Prasanth et al. 2014;Quan et al. 2010;Xu et al. 2008;Zavgorodnya et al. 2017).
Many attempts have been devoted to achieve an effective and eco-friendly solvent for electrospinning cellulose. The different solvent systems used in wetor dry-jet-wet spinning processes, including NMMO/ water, lithium chloride/dimethylacetamide (LiCl/ DMAc), NaOH/urea, and DMSO/triethylamine/SO 2 , have also been used for the electrospinning procedure (Bhat et al. 2019;Chen et al. 2017;Thakur et al. 2017;Xu et al. 2018b;Zhang et al. 2017aZhang et al. , 2019b. Swatloski et al. set a milestone for cellulose processing since they first reported a procedure to dissolve cellulose in ILs (Swatloski 2002). Solubility of cellulose in ILs boosted the electrospinning procedure and ILs-based solvents have been proposed as nontoxic and nonflammable media (Bhat et al. 2019;Hou et al. 2016;Zhang et al. 2019b). However, due to its high viscosity and nonvolatile nature, electrospinning of a cellulose/ILs solution is challenging and it is not easy to control. During the electrospinning process, the solvent has to be removed completely from the fibers. Partial solvent removal can result in fiber fusion, and fiber deposits tend to collapse and agglomerate. ILs cannot evaporate completely between the electrospinning nozzle and the collector due to their low volatility. Hence, to control the morphology of the electrospun fibers, an additional process is required (Härdelin et al. 2012;Prasanth et al. 2014;Teixeira et al. 2020). A coagulation liquid medium such as alcohol or water has been proposed to remove the IL from deposited cellulose nanofibers (Udangawa et al. 2019;Ye et al. 2016;Zheng et al. 2014). Viswanathan et. al (Viswanathan et al. 2006) for the first time, conceived the electrospinning of biopolymeric fibers from room temperature ILs. Electrospun fibers from cellulose/[Bmim]Cl solution was deposited into an ethanol bath, which acted as coagulant for cellulose. However, due to the high viscosity of the cellulose/ [Bmim]Cl solution and low volatility of [Bmim] Cl, cellulose fibers produced during this procedure achieved diameters in the range of microns.
The schematic of typical electrospinning process of cellulose based on ILs is represented in Fig. 12. The setup consists of a high-voltage power supply, a syringe nozzle, and a coagulation bath collector. A syringe pump is used to provide a constant flow rate of the cellulose/IL to feed a droplet at the tip of the nozzle. The electrically-charged jet is ejected from the tip of the Taylor cone, and it is drawn towards the grounded conductive coagulation bath collector within the electrical field. The residual IL is removed from the electrospun fibers by passing through a coagulation bath. Cellulose fibers slowly solidify in the coagulation bath in which the IL is replaced by a coagulant solvent like water or alcohol. This solvent is then removed from these hydrogel fibers by either standard desiccation or freeze-drying (Bazbouz et al. 2019;Frey 2008;Mahmood et al. 2017;Zheng et al. 2014). Parallel copper wires rotating drum or a rotating cylinder partially submerged in a coagulation bath, have been also used as collectors (Härdelin et al. 2013;Işık et al. 2015). In addition, researchers have developed a system for melt-electrospinning or modified the process by incorporating the temperature Fig. 12 Schematic illustration of the electrospinning setup used in the production of cellulose nanofibers from ILs control at the spinneret, at the collector, or at the coagulation bath (Liu et al. 2017;Prasanth et al. 2014;Quan et al. 2010;Xu et al. 2018b).
Many factors and variables can alter the ultimate characteristics of fibers obtained via the electrospinning of cellulose/ILs solution and thus their feasible applications. The control of the effective factors within the electrospinning procedure (e.g., solution properties, process variables, coagulant liquid features, and ambient conditions) needs to be pursued to gain cellulose nanofibers with a specific morphology, diameter, crystallinity, and surface characteristics. Several attempts to optimize the electrospinning process to fabricate cellulose nanofibers from ILs have been performed. Table 6 reviews and summarizes published works regarding the electrospinning of fibers from native cellulose dissolved in ILs.
Research attempts pursue different approaches. Several works have been performed to prevail the challenges of spinnability of cellulose/ILs solutions. Such researches have suggested to use a co-solvent beside ILs to modulate the viscosity, and surface tension of the solvent, to decrease the entanglement density of the system, and to enhance electrical conductivity, and processability of cellulose in the solvent (Ahn et al. 2012a;Freire et al. 2011;Härdelin et al. 2012;Quan et al. 2010;Xu et al. 2008). In some other experimental works, the parameters affecting the spinning process and structural morphology of cellulose/IL electrospun fibers, including the type of the cellulose (Ahn et al. 2012b;Bazbouz et al. 2019;Kang et al. 2013;Polaskova et al. 2013), solution features (concentration and viscosity, cellulose molecular weight, IL solvent system) (Ahn et al. 2012a;Freire et al. 2011;Härdelin et al. 2012;Quan et al. 2010;Xu et al. 2008), and coagulation parameters (coagulant liquid type, immersion time, and method to collect and solidify the fibers) (Bazbouz et al. 2019), have been investigated.
Solution conductivity has an important impact on controlling the electrospinning process and fiber properties and, in view of this, ILs as solvents have the advantage to form the ultrathin and uniform fibers due to their high conductivity. However, high viscosity and surface tension of cellulose/ILs solutions lead to non-uniform beaded fibers. Depending on the molecular weight, polymer solutions can be electrospun within a specified concentration range. An optimal solution concentration gives an adequate viscosity for the formation of continuous uniform bead free fibers (Bazbouz et al. 2019). Quan et al. (2010) reported that the diameter and morphology of the electrospun cellulose fibers were affected by the concentration of cellulose in the IL ([Bmim]Cl) by influencing the viscosity of the solution. The resulting fibers electrospun from the [Bmim]Cl solutions with different cellulose contents were observed via SEM, as shown in Fig. 13. The low cellulose concentration (1.5 w%) showed the lowest viscosity and led to the formation of massive blocks with only a few cellulose fibers. When the concentration increased to 2.4 w%, numerous fibers were formed while, as the solution concentration reached 3 and 4 w%, the blocks disappeared, and fine fibers were achieved. However, when the concentration was raised to 5 w%, the viscosity increased significantly and the fibers with large diameters were formed.
The temperature-controlled electrospinning has been also reported as an effective method to eliminate high viscosity and surface tension limitation of cellulose/ILs solutions by applying an enclosure with a constant temperature surrounding the nozzle. Viscosity and surface tension of the spinning solution decrease at high temperatures (Foong et al. 2020). The melt electrospinning is also another option to minimize the viscosity of spinning solutions. Xu et al. applied a laser-heated melt-set up to generate ultrafine cellulose fibers. They proposed a green and highly efficient process consisting the steps of cellulose dissolution, gel preparation, melt-electrospinning, and fiber coagulation (Xu et al. 2018b).
Another approach to reduce the viscosity and surface tension of cellulose/ILs solutions is to incorporate co-solvents. The effect of co-solvents on the electrospinning of cellulose nanofibers from ILs has been studied by several researchers (Table 6). Härdelin and coworkers performed electrospinning of cellulose pulp from ILs with three different co-solvents: dimethyl acetamide (DMAc), DMF, and DMSO (Härdelin et al. 2012). The goal was to make a relevance between the solution parameters (e.g., viscosity, surface tension, and conductivity) and spinnability in the presence of co-solvent. Results showed that pure [Emim][Ac] did not give the desired fiber formation. The DMSO-based system exhibited higher viscosity values compared to the DMAc-and DMF-based systems, and fibers were formed at a broader interval of [Emim]OAc ratios. Hence, the solution is spinnable   (Fig. 14). The effect of blend ratio of [Amim]Cl and DMSO, as the proposed co-solvent, was investigated by Xu et. al. (2008). They found that the addition of DMSO to cellulose/[Amim][Cl] as co-solvent significantly decreased the surface tension, entanglement density of the network, and while the viscosity of the spinning solution improved the electrospinnability of the solution dramatically. At equal blend ratio of [Amim] Cl/DMSO, the solution was too viscous to be electrospun and no fibers were formed. By increasing the [Amim]Cl/DMSO ratio to 1:2 and 1:4, very stable jets were formed and continuous fibers with diameters in the ranges of 500-800 nm and 100-300 nm were produced, respectively (Fig. 15). At a high [Amim]Cl/ DMSO ratio of 1:8, instead of fiber formation, electrospray occurred.
Therefore, a balance between the parameters, such as polymer concentration, viscosity, surface tension, conductivity, and co-solvent contribution, is necessary for controlling the process to obtain uniform cellulose nanofibers with desired morphology and properties. Literature reviews have proven that the coagulant liquid type is also an important factor affecting the final properties of the nanofiber deposits. The effects of coagulation parameters (coagulation type and time) on the electrospun cellulose fiber structures, have been explored in several works (Bazbouz et al. 2019;Foong et al. 2020;Miyauchi et al. 2011;Quan et al. 2010). Results have shown that spinnability, morphology, and structure of fibers are mainly affected by the procedure used to collect and solidify them. It has been indicated that coagulant liquids owning to different polarities, lead to form fibers with different structural properties such as morphology, porosity, and crystallinity. When water was used as a coagulation bath, due to the relatively slow IL extraction speed of water, ribbon fiber morphology was observed. Also, in some cases, it was observed that cellulose fibers were deposited on the surface of the water bath, and piled up. Thus, wet cellulose fibers merged with each other like a film. In contrast, ethanol was observed a good solvent remove ILs from  (Xu et al. 2008) cellulose fibers, more effective than water. However, ethanol is highly flammable, thus mixture of water/ ethanol can reduce the fire hazard as well as enhance the ILs kinetic removal from the fibers. Cylindrical fiber morphology was obtained in the mixture of water and ethanol (50:50 w/w) coagulation bath. To avoid fiber agglomerations, surfactants can be added to the coagulation bath. Recirculation of coagulant, and using rotating collector for alternative immersion of fibers in a coagulation bath are other suggested routs for fiber collection and to remove the non-volatile solvent from the electrospun fibers (Foong et al. 2020;Meli et al. 2010;Xu et al. 2008).

Electrospinning blend fibers
Aiming at improving the electro-spinnability of cellulose, or exploiting synergistic effects of different polymers for giving special properties, other materials can also be blended besides cellulose to obtain hybrid nanofibrous structures with advanced functions. In general, solution blending is only possible if a common solvent between cellulose and other components of the blend be selected. Finding a common solvent for blending components during the process can be problematic. Hence, multi-jet electrospinning is another method to produce blended fibrous structures in which, the various components are electrospun independently (Le Corre et al. 2014;Zhang et al. 2019b). Among the progresses of cellulose-based hybrids prepared by electrospinning, the blending of polysaccharides, such as chitosan and heparin has gained attention for diverse applications, especially in the biomedical field. Viswanathan et al. (2006) used an electrospinning setup to produce cellulose-heparin blended fibers using ILs. Different solutions of cellulose/[Bmim]Cl and heparin/1-ethyl-3-methylimidazolium benzoate [Emim]Bz were separately prepared and, prior to the electrospinning, both RTIL solutions were mixed to afford a clear cellulose-heparin solution. Fibers were then collected in an ethanol coagulation bath. The electrospun blended fibers were used to design artificial vessels with excellent blood compatibility. In a report by Park et al. (2011b), chitosancellulose hybrid fibers from an IL was demonstrated for the first time.
[Emim]OAc used for dissolving both cellulose and chitosan, and the blend solution was directly electrospun in the ethanol coagulation bath. The electrospun chitosan-cellulose hybrids had a potential application as antimicrobial materials for wound dressing in the biomedical field or for food coatings.
In another research work ), cellulose-based hybrid fibers were produced by electrospinning from blend solutions of cellulose-chitosan and cellulose-PMMA in [Emim][Ac] for wound healing applications. Due to the hydrophobic nature of PMMA, DMF and DMSO were used as co-solvents. The electrospun hybrid fibers were collected into a coagulation distilled water bath to remove [Emim] OAc and to solidify the fibers. A recently published work (Zhang et al. 2019b), suggested a new procedure for the fabrication of micro-fibrillated cellulose fibers through the immiscible blending of PAN and cellulose in [Bmim]Cl. The electrospinning of PAN/ cellulose using [Bmim]Cl, followed by a removal of the PAN phase, allowed obtaining fine cellulose fibers with smaller diameters. This method made possible to control the size of the cellulose fibers and the porosity of the cellulosic matrix by changing the cellulose/PAN blend ratios. Research attempts to electrospun cellulose-based blend fibers are summarized in Table 6.
Co-axial electrospinning approach to produce coreshell fibers Pharmaceutical and food industries are large consumers of cellulosic materials in a multitude of different applications. Hence, there has been interest in using coaxial electrospinning of core-shell type structures based on cellulosic materials to develop new types of composite nanofibrous materials with advanced functions. Coaxial electrospinning has taken advantages of two components in the core and shell layers, and it is possible to add fillers or encapsulate nanoparticles, drugs, bioactive agents, or other nanomaterials for giving special properties, i.e., antibacterial, biological, mechanical, conductivity, etc. (Miyauchi et al. 2010;Thakur et al. 2017). Different materials have been embedded in a cellulosic shell using coaxial electrospinning of IL-based solutions (Table 6). Miyauchi et al. used the coaxial spinneret for electrospinning [Emim]OAc-based solutions to incorporate MWNT in a cellulose shell to produce conductive fibrous materials (Fig. 16) (Miyauchi et al. 2010).
In a recently published work (Udangawa et al. 2019), a coaxial electrospinning setup was used to produce coconut oil-cellulose beaded microfibers as temperature-regulating fibrous materials. [Emim] OAc was chosen as the solvent to prepare the cellulose solution. Phase-change material coconut oil was incorporated inside the cellulosic sheath while the mixture of ethanol-water coagulation bath was used for collecting the core-shell fibers. Figure 17 shows the morphology of the electrospun fibers.
The cellulose monolithic fibers exhibited a cylindrical structure (Fig. 17a) with an average diameter of 600 ± 200 nm. In contrast, core (coconut oil)-shell (cellulose) fibers showed a beaded structure with intermittent cylindrical and biconical shaped zones (Fig. 17b). The core-shell structure of the coconut oil-cellulose fibers was confirmed in images (Fig. 17c).

Applications of cellulose fibers
Cellulose-based materials have been recently developed for a wide range of uses in various fields and several commercial and industrial applications. A general description of the recent eco-friendly applications of cellulose fibers with a focus on biomedical uses is provided in this section. Cellulose is mostly adopted by the paper and packaging industries to replace the use of synthetic polymers derived from petrochemical resources. Cellulose composites are cost effective and non-toxic by nature, hence they can be an important component towards developing biodegradable packaging for food industry applications (Ghaderi et al. 2014;Mu et al. 2019;Sharma et al. 2019).
The potential application of cellulose and its biocomposites have been also largely considered in other fields such as the construction of structural composites, filtration devices, electronics, and sensors (Bethke et al. 2018;Orelma et al. 2020;Sharma et al. 2019).
Nanocellulose with high strength, nanoscale dimension, and large surface area with gas and water barrier properties is a promising material for the fabrication of high-performance membranes and filters. Owning to these properties, environmental applications have been explored, e.g., adsorption of heavy metals and dyes, removal of contaminants, and purification of industrial and drinking water systems (Salama 2019;Wang 2019).
After being extracted from natural sources, regenerated cellulose fibers can be transformed and used in a variety of shapes (e.g., filament or staple fibers, yarns, fabric, nonwovens, membranes, etc.) and applications. The cellulose fiber-based materials are showing a remarkable interest in the last years and a successive growth is expected by an increasing demand in sectors of medical and health products, technical applications, and household products. Cellulosic fibers possess unique properties in moisture control, thus enabling the human body to adapt properly its temperature and give a comfortable feeling when textiles are used in direct skin contact. This feature, which is advantageous for many textile and clothing applications, might explain the rapid production growth of regenerated cellulosic fibers over synthetic fibers. Staple fibers are still the market-leading bulk product for textiles and nonwovens. The good performance of the yarns spun from staple cellulosic fibers during knitting and weaving procedures confirmed the competitive quality of suitability for the production of apparels, therefore suggesting the IL-based cellulosic fibers as an alternative to viscose and Lyocell for production of fabrics and garments (Michud et al. 2016b). Dry-jet wet spinning was used to produce filaments from cellulose/IL solution. The continuous filaments were also cut to staple fibers and compared to the commercial viscose fibers. Staple fibers were converted into yarns by ring spinning technology. The application of cellulose-based fibers is widely reported in the literature. A general description of the recent eco-friendly applications of cellulose fibers with a focus on biomedical uses is provided in this section. Renewable sources, biodegradability, biocompatibility, hydrophilicity, and low toxicity are the intrinsic features of cellulose that make it a suitable candidate for biomedical applications (Abdul Khalil et al. 2020;Teixeira et al. 2020;Thakur et al. 2017). Cellulose fiber-based materials owning to their tunable chemical, physical, and mechanical properties have been widely studied for developing biomaterials such as tissue engineering scaffolds, drug delivery systems, wound dressings, and artificial skin or artificial blood vessels (Abdul Khalil et al. 2020;Courtenay et al. 2018aCourtenay et al. , 2018bCzaja et al. 2006).
Cellulose biocomposites are good candidates for tissue engineering scaffolds due to their suitable mechanical strength and biocompatibility (Palaninathan et al. 2018;Petersen and Gatenholm 2011;Zhijiang et al. 2019). Regenerated cellulose fibers also have been used for creating three-dimensional tissues with capillaries (Ko and Iwata 2001) and for cardiac (Entcheva et al. 2004), bone (Ao et al. 2017;Zhang et al. 2019d), muscle (Jia et al. 2013) and tooth (He et al. 2015;He et al. 2014) tissue engineering. However, when fabricating cellulose fibers, the toxicity of ILs has to be considered since residuals of ILs may end up in the body of patient. For this reason, IL-based biomaterials will be offered to the market if IL impurities do not adversely affect the health. For example, ILs with fluorine-based anions may expose toxicities on many various organisms (Zhao et al. 2007). Thus, ILs used to process biomaterials must be nontoxic, and have to possess also low melting points and low viscosities to be efficient solvents for the biopolymers. Viswanathan et al. (2006) used RTILs to produce electrospun cellulose and celluloseheparin composite fibers for constructing the artificial vessels with excellent blood compatibility.
Cellulose has been considered to condense drugloaded matrices as suitable tablets for oral usage. Despite the long history of application in tableting, there is still research about the use of cellulose as a novel drug delivery system. Nanocellulosebased materials such as hydrogels, microspheres, and fibrous membranes have been also exploited as drug carriers (Abdul Khalil et al. 2015a;Lin and Dufresne 2014;Mishra et al. 2017). Electrospinning is an impressive and beneficial method to develop cellulose-based nanofibrous drug delivery systems with high efficiency. Different types of drugs can be easily entrapped into the electrospun structures with high encapsulation efficiency, and their release behavior can be altered by controlling the morphology, diameter, porosity, and the composition by changing the process variables and type of materials. Several approaches such as post-spinning modifications, electrospinning of drug/polymer blend solution, emulsion electrospinning, and core-shell electrospinning have been proposed to incorporate drug into electrospun cellulose matrix (Liu et al. 2017;Thakur et al. 2017).
Cellulose-based fiber materials have been also proposed as skin wound dressings (Fu et al. 2013;Li et al. 2015a, b). These materials have high water retention capacity to provide the proper moisture at the wound site. Adequate mechanical strength, high permeability and conformability, and low toxicity are other favorable features as temporal biologic dressings. Several studies have focused on pre-clinical and clinical trials of bacterial cellulose (BC) and of nanocellulose derived from plants for wound dressing (Czaja et al. 2006;Hakkarainen et al. 2016). Preclinical tests of nanocellulose scaffolds with high porosity exhibited an accelerating healing process in rats compared to common gauzes with low porosity (Li et al. 2015b). The inflammatory response was also less intense when wounds were covered with BC dressings. Owning to their efficiency, some of the BC wound dressings are already commercially available. For example, wound dressings with brands of Bio-fill® and Bioprocess® are currently commercially offered to treat burns and ulcers. Gengiflex® has been proposed for periodontal diseases, and XCell® has been commercialized for chronic wound care (Czaja et al. 2006;Fontana et al. 1990). Nanofibrillar cellulose (NFC) derived from wood has been also considered as a biological dressing on burn lesions, where split-thickness skin wounds are originated after skin removal (Hakkarainen et al. 2016).

Concluding remarks and future perspectives
While scalable manufacturing is the bottleneck for technology development of many nanoscale materials, fibrillated cellulose provides an approximately unlimited resource for functional materials, since cellulose is produced daily by nearly 3 billion trees and other plants, such as bamboo and sugarcane (Li et al. 2021). Over the last decades, researchers have discovered cellulose as a promising candidate for many applications, and its commercialization in a wide range of products has accelerated. This acceleration comes from consumers' increasing awareness of sustainability and renewability and global regulatory policies. Hence, great efforts have been made to manufacture and develop more efficient and applicable fiber-based cellulosic materials for diverse applications. Among different producing methods, fiber spinning including wet-, dry-, and electro-spinning have been considered as the most suitable, due to their versatile parameters and settings for achieving different fiber sizes, morphologies, and structures.
Although there have been rapid progresses and developments in manufacturing man-made cellulose fibers, some challenges still exist. Researchers have been working to achieve more sustainable and environmentally-friendly man-made cellulose fibers through the application of ILs as green solvents during different fiber spinning procedures. With reduced production costs and increased yields, ongoing growth in fibrillated cellulose production is anticipated as a sustainable material to meet global challenges.
Funding Open access funding provided by Università di Pisa within the CRUI-CARE Agreement.

Conflicts of interest All authors declare no conflict of interests.
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