Baixe o app para aproveitar ainda mais
Prévia do material em texto
Available online at www.sciencedirect.com ScienceDirect Current Opinion in Green and Sustainable Chemistry Green solvents for sustainable separation processes Boelo Schuur, Thomas Brouwer, Dion Smink and Lisette M. J. Sprakel Solvent-based separation processes can reduce the required energy input for separation, improve biocompatibility, and allow for mild responsive separation systems that are applicable when distillation is technically not feasible because of the delicate nature of (bio)molecules to be separated. Owing to the increasing awareness of the need for a green and sustainable industry, the interest in green solvents for separation pro- cesses is growing. Being able to tailor solvent properties and solvent biocompatibility are key properties for making pro- cesses sustainable and allowing flexibility regarding feed and product composition of the separation processes involved. This work aims to give an overview of solvent developments toward more sustainable and green separation processes. For all solvent systems, it is key that not only the primary sepa- ration operation is considered, but the entire process including solvent recovery, because that is typically where the energy should be invested. Addresses Sustainable Process Technology Group, Process and Catalysis Engi- neering Cluster, Faculty of Science and Technology, University of Twente, The Netherlands Corresponding author: Schuur, Boelo (b.schuur@utwente.nl) Current Opinion in Green and Sustainable Chemistry 2019, 18:57–65 This review comes from a themed issue on Green Solvents Edited by Mara G. Freire and João A. P. Coutinho Available online 4 January 2019 https://doi.org/10.1016/j.cogsc.2018.12.009 2452-2236/© 2019 Elsevier B.V. All rights reserved. Introduction The societal awareness of the need to manufacture goods in a sustainable fashion with preferably no to little CO2 emissions is a strong driver to develop new pro- cesses and improve existing ones. This also holds for a range of industries where separations are key and CO2 emissions are significant, that is, the oil industry, the chemical industry, the mining industry, the food in- dustry, and the pharmaceutical industry. In (bio)chem- ical industries, typically around 50% of the energy costs are due to separations [1,2], and with improving these separations, a major contribution to a smaller CO2- footprint can be achieved. With the rise of the petroleum-based economy in the twentieth century, distillation towers have been erected as the working www.sciencedirect.com C horses for separations. Although effective, distillations are often highly energy intensive [1] and solvent-based separations might replace them. Another reason why solvent-based separations become more important is the transition from the oil refinery to the biorefinery. For the highly complex biomass streams, distillation is often not technically feasible and solvent-based separation stra- tegies may be the only option or the most appropriate option. Not seldom, solvent-based biomass fractionation includes reactive fractionation, for example, depoly- merization of lignocellulose [3]. Next to the CO2-foot- print, also other aspects of solvents should be considered such as (eco)toxicity [4]. Another very important solvent-based separation technique is liquide liquid extraction (LLX). LLX is often operated in countercurrent mode in columns, as displayed in Figure 1. Biphasic systems are typically schematically represented as in Figure 1a, whereas the multistage countercurrent operation in the column is displayed in Figure 1c. Stage performance is nowadays computed with thermodynamic models, but ternary diagrams are still common for illustration purposes Figure 1d. An important trend in research on LLX is the use of switchable solvents of which properties such as polarity can be manipulated with external stimuli Figure 1b. We have identified ‘aqueous solvent systems’, ‘ionic liquids (ILs)’, ‘deep eutectic solvents (DESs)’, ‘bio- based solvents’, and ‘switchable solvent systems’ as main solvent classes in which key developments have taken place over the years 2016e2018 that can help the industry become greener and leaner. In the following subsections, each of these classes is discussed in detail and we conclude with an outlook ‘how green, how sustainable?dtoward more sustainable separations’. Aqueous solvent systems A solvent that is generally considered safe, nontoxic, and environmentally friendly is water. Especially for biochemical separations for nutraceutical and pharma- ceutical applications, aqueous systems are of interest, because organic solvents often are not safe enough [5]. However, for many systems, the properties of water are not appropriate for the intended separation, and there- fore, many types of composite solvents based on water have been developed such as aqueous two-phase systems (ATPSs) [6], also used to make cloud point extraction systems [7], hydrotrope forming solutions [5], and aqueous solutions of CO2-switchable solvents [8]. urrent Opinion in Green and Sustainable Chemistry 2019, 18:57–65 mailto:b.schuur@utwente.nl https://doi.org/10.1016/j.cogsc.2018.12.009 http://crossmark.crossref.org/dialog/?doi=10.1016/j.cogsc.2018.12.009&domain=pdf www.sciencedirect.com/science/journal/24522236 www.sciencedirect.com/science/journal/24522236 Figure 1 Current Opinion in Green and Sustainable Chemistry Schematic overview of countercurrent liquid– liquid extraction process (c), where two liquid phases are in equilibrium (a). Dimensioning of such pro- cesses requires proper equilibrium description, for which ternary diagrams are illustrative (d). Stimuli responsive solvents may be applied to facilitate mild solvent regeneration (b). 58 Green solvents Cloud point extraction systems are aqueous surfactant solutions with temperature responsive critical aggrega- tion behavior. Below the critical temperature, micelles are formed that can solubilize hydrophobic species, and above the critical temperature, the micelles break up, inducing a macroscopic phase split which allows for product recovery. Recently, cloud point extraction sys- tems have been reported for extraction of lipids from microalgae [9], which due to the low toxicity appears to be a solution that may be applied for microalgae bio- refineries with food applications [7]. Next to solubilization in surfactant systems (Figure 2a), it is also possible to use amphiphilic molecules or ions containing a hydrophobic moiety not large enough to form micelles on their own but can form hydrotropes together with hydrophobic species in solution (see Figure 2b). De Faria et al. [5]** showed that extremely hydrophobic species (triterpenes) may be solubilized in aqueous so- lutions of surface active ILs, enhancing their solubility up to eight orders of magnitude. This remarkable solu- bility enhancement may be applied in other fields such as pharmaceutical engineering where aqueous solubil- ities of steroids may be boosted similarly to enable much more sustainable processing than with traditional (halogenated) organic solvents. Another recent advance Current Opinion in Green and Sustainable Chemistry 2019, 18:57–65 involving hydrotropic solutions was the microwave- assisted phytoextraction of geraniol [10], where due to the combination of microwave action and hydrotropes, a much shorter extraction time could be achieved. ATPSs are solvent systems consisting of two aqueous phases that are at least partially immiscible. The degree of immiscibility is expressed by the tie-line length, and systems with long tie-line length exhibit a limited mutual miscibility. Immiscibility of aqueous phases is due to the repulsive behavior of its main constituents, for example, a salt and a polymer or two polymers, or an ionic liquid and a polymer or a salt [6]. Because both phases are water-based, very mild separations can be performed without disrupting biomolecules of interest, for example, monoclonal antibodies, enzymes, and vi- tamins. Recentwork in this field is strongly emphasized on the use of ILs, for increased polarity and specific interactions [11], biocompatibility [12], induced salting out effects for selective separations [13], and induced response to external stimuli such as temperature [12] and pH [14]. Ionic liquids ILs are salts that are liquid at T < 100 �C, and by changing the structure of either the organic cation and/ or the organic or inorganic anion, the ion properties can www.sciencedirect.com www.sciencedirect.com/science/journal/24522236 Figure 2 Current Opinion in Green and Sustainable Chemistry The schematic representation of (a) micellization by sodium dodecylsulphate and (b) the formation of a hydrotrope by 1-butyl-3-alkylimidazolium, surrounding ursolic acid. The blue and red areas on the solvent molecules indicate a polar and apolar functional group, respectively. Green solvents for sustainable separation processes Schuur et al. 59 be tailored. An often praised property is their negligible vapor pressure that prevents solvent losses through evaporation. ILs form the solvent class that received by far the most attention in the past decade [3,6,15]. ILs have been applied in a wide range of processes, including many separations such as analytical separa- tions [16,17], aromatic-aliphatic separation [18,19], carbon capture [15], metal extractions [20,21]*, acid extractions [22], and biomass fractionations [3]. In our opinion, the biggest hype around ILs is over now, and critical articles are also welcomed that bring the use of ILs in perspective and compare with traditional sol- vents, for example, for aromatic-aliphatic separation [18]. Indeed, we are convinced that, for many applica- tions, ILs can be very beneficial but they are not the www.sciencedirect.com C perfect solution to everything and too enthusiastic claims should be considered with caution. For example, ample literature is available on CO2-capture using ILs, and recently, several claims (myths) about physical sol- ubility of CO2 in ILs were dispelled in an excellent article by Carvalho et al [23]**. Next to the physical solubility, in our opinion, the fact that the total ab- sorption capacity including both physical and chemical absorption for state-of-the-art IL-based absorption sys- tems does not exceed 1 mol of CO2 per mol of ion pair [24] should be regarded critically, as traditional amine solvents reach similar values [25] and typically exhibit a lower molar mass. Nevertheless, in comparison to aqueous solutions of volatile amines, regeneration of ILs may be much greener and cheaper by avoiding volatile urrent Opinion in Green and Sustainable Chemistry 2019, 18:57–65 www.sciencedirect.com/science/journal/24522236 60 Green solvents amine emissions and reducing water evaporation. However, viscosity may severely affect heat transfer and mass transfer, which were identified as key challenges for use of ILs as CO2 capture solvent because they can result in absurd requirements for column heights as shown in Figure 3 [26]**. Also, for separation of aliphatics and aromatics, huge numbers of articles have appeared just reporting distri- bution coefficients. It is key that also other important aspects are considered, such as overall process efficiency and toxicity, as was performed in an excellent combination by Dı́az et al. [27]*. Metal extractions with classical molecular solvents have been studied and industrially applied for decades, often using kerosene as a diluent, intrinsically posing a risk due to the flammability. This field may benefit from the development of IL-based separation systems for metal extractions in terms of safety. In the most recent years, a new dimension has been added to metal extractions, that is, urban mining, meaning that recycling of metals from end-of-life electronics is aimed [21]*. Given that the average lifetime of electronic devices such as cell phones is nowadays only a few years and these devices contain many elements, fractionations of (rare) metals Figure 3 Required column heights for CO2 capture with several ILs in perspective. Repro The Royal Society of Chemistry. Current Opinion in Green and Sustainable Chemistry 2019, 18:57–65 from electronic waste are of key importance for our so- ciety. The article by Li et al [21]* offers an excellent approach for metal fractionation, whereas another key article authored by Gras et al [20]** shows excellent extraction yields for several metals using IL-based ATPS, intrinsically safe and a potential breakthrough not only for urban mining but also for the traditional mining industries. In the field of biorefinery applications of ILs, the most important recent developments include lignin depoly- merization [28], nanocellulose production [29], and fractionations from aquatic biomass such as microalgae [30]**. The article by Desai et al. [30]** describes a microalgae biorefinery in which both pigments and proteins are fractionated from the algae biomass in a single stage using microgel particleestabilized IL emulsions. In the absence of the microgel particles, the protein was less stable. It is envisioned that this approach may be much wider applicable in biorefineries to prevent denaturation of sensitive molecules during fractionation. Next to hydrophobic ILs stabilized by microgel particles, IL-based ATPS also might be applied to obtain mild systems able to fractionate proteins, for example, from carbohydrates [31]. Current Opinion in Green and Sustainable Chemistry duced from Ref. [26]**—Published under Creative Commons license by www.sciencedirect.com www.sciencedirect.com/science/journal/24522236 Figure 4 Current Opinion in Green and Sustainable Chemistry Examples of molecules that are frequently applied in DESs. Often they are designated as hdyrogen bond acceptor (HBA) or as hydrogen bond donor (HBD), but many can be both donating and accepting hydrogen bonds. Green solvents for sustainable separation processes Schuur et al. 61 Deep eutectic solvents DESs are composite solvents that exhibit deep eutectic behavior, that is, upon mixing the constituents of these solvents, the mixtures’ melting points reduce consid- erably more (>50 �C) than would be the case for ideal mixtures. Deep eutectic behavior is typically observed by mixing hydrogen bonding constituents, and by vari- ation of hydrogen bond acceptor and/or hydrogen bond donor, these solvents are tunable like ILs are tunable by variation of ions. DESs, and in particular, natural DESs (NADESs) [32,33] have been claimed to be less toxic, more biodegradable, and significantly cheaper than ILs [34]. Although in our opinion caution should be applied upon making strongly generalized statements with regard to toxicity and biodegradability, in many exam- ples these properties do apply. Furthermore, owing to their tremendous combination possibilities, this solvent class can also be considered a designer solvent class and numerous applications have already been explored. Ex- amples are pretreatment of lignocellulosic materials without cellulase deactivation [35], enhanced fraction- ation of lignocellulosic materials [36], and urban mining of nickel and cobalt [37]. In the field of mild separation, DESs have been applied for proteins separation, both with DES-coated magnetic nanoparticles [38] and in DES-based ATPS systems [39]. Because the properties of DES are not only dependent on their molecular structures but also strongly on the ratio in which they are present in a fluid phase, the stability of ATPS from DESs might be limited to certain combinations [40]. More conventional processes, such as sulfur removal [41], aliphatic/aromatic separations [42], and CO2 cap- ture [43] have also been evaluated. For CO2-capture high equilibrium capacity was found to compromise with viscosity [44], an aspect that should be considered with care, because, for ILs, viscosity was found to be a very critical parameter [26]**. Using hydrophobic DESs impregnated in a membrane, furans could be separated from aqueoussolutions [45]*. Similar to ILs, also most (NA)DESs reported in literature are hydrophilic, but these hydrophobic examples (see Figure 4) offer in our opinion highly interesting options for future research on recovery of bio-based chemicals from dilute aqueous streams. From the diversity of already reported applications and the outlook on future possible applications, it may be concluded that (NA)DESs are comparably versatile as ILs while also highly compatible with a circular econ- omy, as displayed in Figure 4 and are expected to receive ample attention in the coming years. Bio-based solvents Besides NADESs, other highly interesting biodegrad- able and nontoxic bio-based solvents have recently been evaluated for various separations where they exhibited often comparable properties to conventional solvents. www.sciencedirect.com C Examples of bio-based solvents include Cyrene [46,47], 2-methyltetrahydrofuran [47], g-valerolactone [47], and methyl(2,2-dimethyl-1,3-dioxolan-4-yl)methyl carbon- ate [48]. Recently, access to a rich variety of Cyrene derivatives was reported, and a new solvent class called Cygnet x.y appears as a potential renewable replace- ment for N-methyl pyrrolidone (NMP) [49]**. The ability to vary the side groups on x and y positions through synthetic modifications (see Figure 5 for structure of Cygnet x.y) [49]** fosters versatility in applicability. Sustainable ILs have also been reported, although they still require conventional solvents in their production process [50]. The use of bio-based solvents is essential in closing the carbon balance for a circular economy, see Figure 5. Switchable solvent systems Solvents that switch their nature reversibly upon an external stimulus can be applied in affinity separation systems where the nature of the solvent during the primary separation is different from the nature in the regeneration stage. Such a switch can aid the regener- ability of the solvent. Temperature-responsive solvents (surfactant based or polymers) are best known [9], but recently also other stimuli get more attention. For example, solvents that switch polarity upon exposure to urrent Opinion in Green and Sustainable Chemistry 2019, 18:57–65 www.sciencedirect.com/science/journal/24522236 Figure 5 Current Opinion in Green and Sustainable Chemistry Examples and circularity of sustainable, nature-derived solvent systems. ATPS, aqueous two-phase system; NADES, natural deep eutectic solvent; MMC, methyl(2,2-dimethyl-1,3-dioxolan-4-yl)methyl carbonate. 62 Green solvents CO2 are considered as very promising for application in several separation and synthesis processes. Pioneered by Jessop et al [51], CO2-switchable solvents (CO2-SSs) have been used in extracting lipids from microalgae [52] and as an entrainer in extractive distillation of heptanee toluene mixtures [53]. Very recently another highly interesting approach was shown by Cicci et al [54]**, who developed the circular extraction concept, in which both states of the solvent were used to extract polar compounds with the ionic form and apolar compounds with the neutral form. When applied in an aqueous so- lution (requiring the neutral state also to be water sol- uble), switching a CO2-SS between its uncharged state and an ionic state switches the ionic strength [12], which allows for reversible salting out of organic com- pounds from water [8]. CO2-SSs are typically based on amines that are not always environmentally benign, making the full solvent life cycle including consider- ations on solvent losses important [12]. To aid the sol- vent screening of CO2 switchable hydrophilicity solvents, a technique using a microfluidic device was Current Opinion in Green and Sustainable Chemistry 2019, 18:57–65 developed by Lestari et al [55] to study the performance and recovery of the solvent, as well as the losses in the process [55]. In addition, redox potential may be applied to switch solvents, and on the basis of work from the Hatton group on redox responsive gels [56], solvents [57], and elec- trodes [58]*, solvents with these specific redox responsive groups may be switched between different states reversibly, allowing electrochemical tuning of their functional group affinity with great potential in the field of carbon capture [57], water purification, and se- lective electrochemical separations [58]*. Other stimuli that may aid separations are magnetism, for example, to collect droplets of magnetic fluids effectively [59] and light. Van Dijken et al [60]** demonstrated that aggregation of photoresponsive am- phiphiles can be photo-controlled and anion binding can be affected with light when photo switching receptors are applied [61,62]**. Such photoresponsive www.sciencedirect.com www.sciencedirect.com/science/journal/24522236 Green solvents for sustainable separation processes Schuur et al. 63 aggregation and binding enables very mild recovery by photo switch. How green, how sustainable?—toward more sustainable separations Following the twelve principles of green chemistry [63], a conscious solvent choice is essential. This requires a balance of solvent function and minimal toxicity and biodegradability (principle 4 and 10) and solvent pro- duction from renewable sources (principle 7). The current trend from conventional solvents and ILs to bio- based solvents, NADESs, and ATPS is usually in accordance with these principles. A key aspect of a sustainable solvent-based separation process develop- ment should be the ease of recovery. When solvents are applied with extremely good distribution coefficients, the energy level of the extract phase may be very low, compromising on the regenerability and requiring large energy input to achieve the ‘separated components’ state. A similar statement was recently formulated for acid extractions as ‘thinking beyond the partition ratio’ [64], and we suggest to always check if sustainability measures conform the green chemistry principles when developing a new solvent-based separation system. Sustainability analysis of solvent-based separation pro- cesses should always include the full process concept, including (bio)compatibility with the chemistry that the solvent is applied to and solvent regeneration. It is key not to consider a solvent that is green and sustainable because it has been identified as such for another application, because a solvent that is sustainable in one process is not necessarily sustainable in another process in terms of (bio)compatibility and regenerability. For the highly innovative switching systems, this means also thinking about the overall energy efficiency of the switching system, including light sources, which may seriously affect the overall process evaluation. Never- theless, such switching systems open pathways to use green electricity as energy source for the regeneration, which can seriously reduce CO2 emission, and may offer a unique mild route that allows product recovery that would otherwise not be possible. Conflict of interest statement Nothing declared.. References 1. Sholl DS, Lively RP: Seven chemical separations to change the world. Nature 2016, 532:435–437. 2. Kiss AA, Lange JP, Schuur B, Brilman DWF, van der Ham AGJ, Kersten SRA: Separation technology–Making a difference in biorefineries. Biomass Bioenergy 2016, 95:296–309. 3. Yoo CG, Pu Y, Ragauskas AJ: Ionic liquids: promising green solvents for lignocellulosic biomass utilization. Curr Opin Green Sust Chem 2017, 5:5–11. 4. Ruokonen SK, Sanwald C, Sundvik M, Polnick S, Vyavaharkar K, Du�sa F, et al.: Effect of ionic liquids on Zebrafish (Danio rerio) www.sciencedirect.com C viability, behavior, and histology; correlation between toxicity and ionic liquid aggregation. Environ Sci Technol 2016, 50:7116–7125. 5. De Faria ELP, Shabudin SV, Claúdio AFM, Válega M, Domingues FMJ, Freire CSR, et al.: Aqueous solutions of surface-active ionic liquids: remarkable alternative solvents to improve the solubility of triterpenic acids and their extraction from biomass.ACS Sustain Chem Eng 2017, 5: 7344–7351. 6. Freire MG, Cláudio AFM, Araújo JMM, Coutinho JAP, Marrucho IM, Lopes JNC, et al.: Aqueous biphasic systems: a boost brought about by using ionic liquids. Chem Soc Rev 2012, 41:4966–4995. 7. Racheva R, Rahlf AF, Wenzel D, Müller C, Kerner M, Luinstra GA, et al.: Aqueous food-grade and cosmetic-grade surfactant systems for the continuous countercurrent cloud point extraction. Separ Purif Technol 2018, 202:76–85. 8. Vanderveen JR, Sarika B, Jialing G, Goyon A, Jardine A, Shin HE, et al.: Characterizing the effects of a “switchable water” additive on the aqueous solubility of small molecules. ChemPhysChem 2018, 19:2093–2100. 9. Racheva R, Tietgens N, Kerner M, Smirnova I: In situ contin- uous countercurrent cloud point extraction of microalgae cultures. Separ Purif Technol 2018, 190:268–277. 10. Thakker MR, Parikh JK, Desai MA: Ultrasound assisted hy- drotropic extraction: a greener approach for the isolation of geraniol from the leaves of cymbopogon martinii. ACS Sus- tain Chem Eng 2018, 6:3215–3224. 11. Sousa RdCS, Pereira MM, Freire MG, Coutinho JAP: Evaluation of the effect of ionic liquids as adjuvants in polymer-based aqueous biphasic systems using biomolecules as molecular probes. Separ Purif Technol 2018, 196:244–253. 12. Clarke CJ, Tu W-C, Levers O, Bröhl A, Hallett JP: Green and sustainable solvents in chemical processes. Chem Rev 2018, 118:747–800. 13. Passos H, Costa SH, Fernandes AM, Freire MG, Rogers RD, Coutinho JAP: A triple salting-out effect is required for the formation of ionic-liquid-based aqueous multiphase systems. Angew Chem Int Ed 2017, 56:15058–15062. 14. Ferreira AM, Claudio AFM, Valega M, Domingues FMJ, Silvestre AJD, Rogers RD, et al.: Switchable (pH-driven) aqueous biphasic systems formed by ionic liquids as inte- grated production-separation platforms. Green Chem 2017, 19:2768–2773. 15. Zeng S, Zhang X, Bai L, Zhang X, Wang H, Wang J, et al.: Ionic- liquid-based CO2 capture systems: structure, interaction and process. Chem Rev 2017, 117:9625–9673. 16. Nacham O, Ho TD, Anderson JL, Webster GK: Use of ionic liquids as headspace gas chromatography diluents for the analysis of residual solvents in pharmaceuticals. J Pharm Biomed Anal 2017, 145:879–886. 17. Patil RA, Talebi M, Xu C, Bhawal SS, Armstrong DW: Synthesis of thermally stable geminal dicationic ionic liquids and related ionic compounds: an examination of physicochem- ical properties by structural modification. Chem Mater 2016, 28:4315–4323. 18. Canales RI, Brennecke JF: Comparison of ionic liquids to conventional organic solvents for extraction of aromatics from aliphatics. J Chem Eng Data 2016, 61:1685–1699. 19. Meindersma W, Onink F, Hansmeier AR, de Haan AB: Long term pilot plant experience on aromatics extraction with ionic liq- uids. Separ Sci Technol 2012, 47:337–345. 20. Gras M, Papaiconomou N, Schaeffer N, Chainet E, Tedjar F, Coutinho JAP, et al.: Ionic-liquid-based acidic aqueous biphasic systems for simultaneous leaching and extraction of metallic ions. Angew Chem Int Ed 2018, 57:1563–1566. 21. Li X, Van den Bossche A, Vander Hoogerstraete T, Binnemans K: Ionic liquids with trichloride anions for oxidative dissolution of metals and alloys. Chem Commun 2018, 54:475–478. urrent Opinion in Green and Sustainable Chemistry 2019, 18:57–65 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref2 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref2 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref3 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref3 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref3 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref4 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref4 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref4 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref5 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref6 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref7 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref7 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref7 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref7 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref8 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref8 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref8 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref8 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref9 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref9 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref9 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref9 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref10 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref10 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref10 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref11 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref11 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref11 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref11 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref12 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref12 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref12 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref12 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref13 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref13 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref13 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref14 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref14 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref14 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref14 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref15 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref15 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref15 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref15 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref15 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref16 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref16 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref16 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref17 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref17 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref17 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref17 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref18 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref18 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref18 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref18 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref18 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref19 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref19 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref19 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref20 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref20 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref20 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref21 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref21 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref21 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref21 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref22 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref22 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref22 www.sciencedirect.com/science/journal/24522236 64 Green solvents 22. Reyhanitash E, Zaalberg B, Kersten SRA, Schuur B: Extraction of volatile fatty acids from fermented wastewater. Separ Purif Technol 2016, 161:61–68. 23. Carvalho PJ, Kurnia KA, CoutinhoJAP: Dispelling some myths about the CO2 solubility in ionic liquids. Phys Chem Chem Phys 2016, 18:14757–14771. 24. Sheridan QR, Mullen RG, Lee TB, Maginn EJ, Schneider WF: Hybrid computational strategy for predicting CO2 solubilities in reactive ionic liquids. J Phys Chem C 2018, 122: 14213–14221. 25. Singh P, Brilman DWF, Groeneveld MJ: Evaluation of CO2 solubility in potential aqueous amine-based solvents at low CO2 partial pressure. Int J Greenh Gas Contr 2011, 5:61–68. 26. Mota-Martinez MT, Brandl P, Hallett JP, Mac Dowell N: Chal- lenges and opportunities for the utilisation of ionic liquids as solvents for CO2 capture. Mol Syst Des Eng 2018, 3:560–571. 27. Díaz I, Rodriguez M, González EJ: Selection of a minimum toxicity and high performance ionic liquid mixture for the separation of aromatic - aliphatic mixtures by extractive distillation. Comput Aided Chem Eng 2017:2209–2214. 28. De Gregorio GF, Prado R, Vriamont C, Erdocia X, Labidi J, Hallett JP, et al.: Oxidative depolymerization of lignin using a novel polyoxometalate-protic ionic liquid system. ACS Sus- tain Chem Eng 2016, 4:6031–6036. 29. Laaksonen T, Helminen JKJ, Lemetti L, Långbacka J, Rico del Cerro D, Hummel M, et al.:WtF-nano: one-pot dewatering and water-free topochemical modification of nanocellulose in ionic liquids or G-valerolactone. ChemSusChem 2017, 10:4879–4890. 30. Desai RK, Monteillet H, Li X, Schuur B, Kleijn JM, Leermakers FAM, et al.: One-step mild biorefinery of functional biomolecules from microalgae extracts. React Chem Eng 2018, 3:182–187. 31. Suarez Garcia E, Suarez Ruiz CA, Tilaye T, Eppink MHM, Wijffels RH, van den Berg C: Fractionation of proteins and carbohydrates from crude microalgae extracts using an ionic liquid based-aqueous two phase system. Separ Purif Technol 2018, 204:56–65. 32. Płotka-Wasylka J, Rutkowska M, Owczarek K, Tobiszewski M, Namie�snik J: Extraction with environmentally friendly sol- vents. Trends Anal Chem 2017, 91:12–25. 33. Liu Y, Friesen JB, McAlpine JB, Lankin DC, Chen S-N, Pauli GF: Natural deep eutectic solvents: properties, applications, and perspectives. J Nat Prod 2018, 81:679–690. 34. Gomez FJ, Espino M, Fernández MA, Silva MF: A greener approach to prepare natural deep eutectic solvents. Chemis- trySelect 2018, 3:6122–6125. 35. Wahlström R, Hiltunen J, Pitaluga de Souza Nascente Sirkka M, Vuoti S, Kruus K: Comparison of three deep eutectic solvents and 1-ethyl-3-methylimidazolium acetate in the pretreatment of lignocellulose: effect on enzyme stability, lignocellulose digestibility and one-pot hydrolysis. RSC Adv 2016, 6: 68100–68110. 36. Liu Y, Chen W, Xia Q, Guo B, Wang Q, Liu S, et al.: Efficient cleavage of lignin-carbohydrate complexes and ultrafast extraction of lignin oligomers from wood biomass by microwave-assisted treatment with deep eutectic solvent. ChemSusChem 2017, 10:1692–1700. 37. Albler F-J, Bica K, Foreman MRS, Holgersson S, Tyumentsev MS: A comparison of two methods of recovering cobalt from a deep eutectic solvent: implications for battery recycling. J Clean Prod 2017, 167:806–814. 38. Xu K, Wang Y, Ding X, Huang Y, Li N, Wen Q: Magnetic solid- phase extraction of protein with deep eutectic solvent immobilized magnetic graphene oxide nanoparticles. Talanta 2016, 148:153–162. 39. Farias FO, Passos H, Sanglard MG, Igarashi-Mafra L, Coutinho JA, Mafra MR: Designer solvent ability of alcohols in aqueous biphasic systems composed of deep eutectic solvents and potassium phosphate. Separ Purif Technol 2018, 200:84–93. Current Opinion in Green and Sustainable Chemistry 2019, 18:57–65 40. Farias FO, Passos H, Lima ÁS, Mafra MR, Coutinho JAP: Is it possible to create ternary-like aqueous biphasic systems with deep eutectic solvents? ACS Sustain Chem Eng 2017, 5: 9402–9411. 41. Alli RD, AlNashef IM, Kroon MC: Removal of 2-and 3- methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents. J Chem Thermodyn 2018, 125:172–179. 42. Warrag SEE, Peters CJ, Kroon MC: Deep eutectic solvents for highly efficient separations in oil and gas industries. Curr Opin Green Sust Chem 2017, 5:55–60. 43. Sarmad S, Mikkola JP, Ji X: Carbon dioxide capture with ionic liquids and deep eutectic solvents: a new generation of sor- bents. ChemSusChem 2017, 10:324–352. 44. Mirza N, Mumford K, Wu Y, Mazhar S, Kentish S, Stevens G: Improved eutectic based solvents for capturing carbon di- oxide (CO2). Energy Procedia 2017:827–833. 45. Dietz CHJT, Kroon MC, Di Stefano M, van Sint Annaland M, Gallucci F: Selective separation of furfural and hydrox- ymethylfurfural from an aqueous solution using a supported hydrophobic deep eutectic solvent liquid membrane. Faraday Disc 2018, 206:77–92. 46. Sherwood J, De bruyn M, Constantinou A, Moity L, McElroy CR, Farmer TJ, et al.: Dihydrolevoglucosenone (Cyrene) as a bio- based alternative for dipolar aprotic solvents. Chem Commun 2014, 50:9650–9652. 47. Vovers J, Smith K, Stevens G: Bio-based molecular solvents. The application of green solvents in separation processes. Elsevier; 2017:91–110. 48. Jin S, Byrne F, McElroy CR, Sherwood J, Clark JH, Hunt AJ: Challenges in the development of bio-based solvents: a case study on methyl (2, 2-dimethyl-1, 3-dioxolan-4-yl) methyl carbonate as an alternative aprotic solvent. Faraday Disc 2017, 202:157–173. 49. Alves Costa Pacheco A, Sherwood J, Zhenova A, McElroy CR, Hunt AJ, Parker HL, et al.: Intelligent approach to solvent substitution: the identification of a new class of levogluco- senone derivatives. ChemSusChem 2016, 9:3503–3512. 50. Hulsbosch J, De Vos DE, Binnemans K, Ameloot R: Biobased ionic liquids: solvents for a green processing industry? ACS Sustain Chem Eng 2016, 4:2917–2931. 51. Jessop PG, Heldebrant DJ, Li X, Eckert CA, Liotta CL: Revers- ible nonpolar-to-polar solvent. Nature 2005, 436:1102. 52. Du Y, Schuur B, Brilman DWF: Maximizing lipid yield in neochloris oleoabundans algae extraction by stressing and using multiple extraction stages with N-ethylbutylamine as switchable solvent. Ind Eng Chem Res 2017, 56:8073–8080. 53. Schuur B, Nijland M, Blahusiak M, Juan A: CO2-switchable solvents as entrainer in fluid separations. ACS Sustain Chem Eng 2018, 6:10429–10435. 54. Cicci A, Sed G, Jessop PG, Bravi M: Circular extraction: an innovative use of switchable solvents for the biomass bio- refinery. Green Chem 2018, 20:3908–3911. 55. Lestari G, Alizadehgiashi M, Abolhasani M, Kumacheva E: Study of extraction and recycling of switchable hydrophilicity sol- vents in an oscillatory microfluidic platform. ACS Sustain Chem Eng 2017, 5:4304–4310. 56. Akhoury A, Bromberg L, Hatton TA: Redox-responsive gels with tunable hydrophobicity for controlled solubilization and release of organics. ACS Appl Mater Interfaces 2011, 3: 1167–1174. 57. Gurkan B, Simeon F, Hatton TA: Quinone reduction in ionic liquids for electrochemical CO2 separation. ACS Sustain Chem Eng 2015, 3:1394–1405. 58. Su X, Hatton TA: Redox-electrodes for selective electro- chemical separations. Adv Colloid Interface Sci 2017, 244: 6–20. www.sciencedirect.com http://refhub.elsevier.com/S2452-2236(18)30091-9/sref23 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref23 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref23 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref24 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref24 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref24 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref25 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref25 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref25 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref25 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref26 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref26 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref26 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref27 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref27 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref27http://refhub.elsevier.com/S2452-2236(18)30091-9/sref28 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref28 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref28 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref28 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref29 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref29 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref29 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref29 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref30 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref30 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref30 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref30 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref31 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref31 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref31 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref31 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref32 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref32 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref32 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref32 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref32 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref33 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref33 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref33 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref33 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref34 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref34 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref34 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref35 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref35 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref35 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref36 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref37 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref37 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref37 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref37 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref37 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref38 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref38 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref38 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref38 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref39 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref39 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref39 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref39 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref40 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref40 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref40 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref40 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref41 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref41 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref41 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref41 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref42 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref42 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref42 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref42 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref42 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref43 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref43 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref43 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref44 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref44 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref44 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref45 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref45 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref45 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref46 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref46 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref46 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref46 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref46 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref47 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref47 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref47 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref47 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref48 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref48 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref48 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref49 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref49 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref49 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref49 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref49 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref50 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref50 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref50 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref50 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref51 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref51 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref51 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref52 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref52 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref53 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref53 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref53 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref53 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref54 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref54 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref54 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref55 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref55 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref55 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref56 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref56 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref56 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref56 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref57 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref57 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref57 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref57 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref58 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref58 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref58 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref58 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref59 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref59 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref59 www.sciencedirect.com/science/journal/24522236 Green solvents for sustainable separation processes Schuur et al. 65 59. Monteillet H, Workamp M, Li X, Schuur B, Kleijn JM, Leermakers FAM, et al.: Multi-responsive ionic liquid emul- sions stabilized by microgels. Chem Commun 2014, 50: 12197–12200. 60. Van Dijken DJ, Chen J, Stuart MCA, Hou L, Feringa BL: Amphiphilic molecular motors for responsive aggregation in water. J Am Chem Soc 2016, 138:660–669. 61. Vlatkovic M, Feringa BL, Wezenberg SJ: Dynamic inversion of stereoselective phosphate binding to a bisurea receptor controlled by light and heat. Angew Chem Int Ed 2016, 55: 1001–1004. www.sciencedirect.com C 62. Wezenberg SJ, Feringa BL: Photocontrol of anion binding af- finity to a bis-urea receptor derived from stiff-stilbene. Org Lett 2017, 19:324–327. 63. Anastas PT, Warner JC: Green chemistry: theory and practice. Oxford University Press; 1998. 64. Shah VH, Pham V, Larsen P, Biswas S, Frank T: Liquid– liquid extraction for recovering low margin chemicals: thinking beyond the partition ratio. Ind Eng Chem Res 2016, 55: 1731–1739. urrent Opinion in Green and Sustainable Chemistry 2019,18:57–65 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref60 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref60 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref60 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref60 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref61 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref61 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref61 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref62 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref62 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref62 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref62 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref63 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref63 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref63 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref64 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref64 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref65 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref65 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref65 http://refhub.elsevier.com/S2452-2236(18)30091-9/sref65 www.sciencedirect.com/science/journal/24522236 Green solvents for sustainable separation processes Introduction Aqueous solvent systems Ionic liquids Deep eutectic solvents Bio-based solvents Switchable solvent systems How green, how sustainable?—toward more sustainable separations Conflict of interest statement References
Compartilhar