Filipa A.
Vicente
*,
Nuša
Tkalec
and
Blaž
Likozar
Department of Catalysis and Chemical Reaction Engineering, National Institute of Chemistry, Hajdrihova 19, 1000 Ljubljana, Slovenia. E-mail: filipa.andre.vicente@ki.si
First published on 11th December 2024
In an era so focused on sustainability, it is important to improve chemical processes by developing and using more environmentally friendly solvents and technologies. Deep eutectic solvents (DES) have proven to be a promising replacement for conventional solvents. In recent years, a new type of DES has emerged that responds to various stimuli. These responsive DES (RDES) may offer all the advantages of DES while allowing the recycling and reuse of solvents. As such, RDES can further contribute to a greener future. This review provides an overview of the diverse types of RDES, their switching mechanisms and their application in several fields. Lastly, it offers a critical perspective on current shortcomings and prospects.
The composition of RDES has a fundamental impact on its role as a solvent in all application processes as well as on the switching mechanism. Thus, a significant amount of research on RDES is focused on understanding and carefully designing the solvent through the selection of HBAs and HBDs that can produce a DES that is responsive to stimuli for specific applications. Fundamental knowledge of the compounds properties as well as thorough research of already successfully produced RDES is key to the development of novel switchable DES for catalysis, downstream processes and other applications.26 A summary of the most selected RDES precursors reported in the literature, as well as the switching mechanism and the RDES research application is presented in Table 1. The HBAs that have so far proved efficient in the production of switchable DES include amines (secondary and tertiary), amidines, quaternary ammonium (salts), guanidine and nitrogenous bases, fatty acids, and phenols. HBDs include fatty acids, phenolic compounds, and alcohols.27–30 The preparation of RDES can be achieved by selecting and combining HBAs and HBDs in a simple and environmentally friendly process that produces no by-products.
Driving factor | DES components (HBA:HBD) | Molar ratio | Conditions | Applications | Ref. |
---|---|---|---|---|---|
a These studies are the most representative over the last 5 years. RT – room temperature. b In this study, several hydrophilic and hydrophobic DES were prepared and combined together with water, which were later applied for the extraction of different compounds from various sources, so the optimal molar ratio changes. | |||||
CO2 | Diethylamine: 1,3-dibromopropane | 1:4 | Stirring at 40 °C | Oil-solid separation | 31 |
Monoethanolamine:4-methoxyphenol | 1:1 | Stirring at RT | Homogeneous liquid–liquid microextraction of chlorobenzenes | 32 | |
Thymol:octanoic acid | 1:5 | Stirring at 70 °C | Determination of fungicides contents in water, juice, wine, and vinegar | 33 | |
Choline chloride:octanoat | 1:2 | Stirring at 65 °C | Valorization of papaya peels for thrombolytic cysteine protease isolation | 34 | |
Imidazole:thylene glycol | 1:1 | Stirring at 30 °C | Phase separation of DES/olive oil emulsion | 35 | |
Choline chloride:octanoic acid | 1:2 | Stirring at 80 °C | Determination of anthraquinones in fried Cassiae semen tea infusions | 36 | |
4-Methoxyphenyl:3-amino-1-propanol | 1:1 | Stirring at 70 °C | Determination of enantiomers of the fungicide mefentrifluconazole in water, fruit juice, and fermented liquor samples | 37 | |
Tetramethylguanidine:menthol | 3:1 | Stirring at 80 °C for 2 h | Extraction of lipids from Nannochloropsis sp. | 38 | |
Monoethanolamine:butanol | 1:1 | Stirring at RT | Recovery and repurposing of waste isopropanol | 39 | |
Triethanolamine:4-methoxyphenol | 1:1 | Stirring at 25–80 °C | Extraction of hesperidin from orange peels | 40 | |
Temperature | Lidocaine:oleic acid | 1:1 | Stirring at 20 °C | Extraction of dyes from water | 30 |
Tetracaine:lauric acid | 1:1 | Stirring at 80 °C | Extraction and separation of Lycium barbarum polysaccharides | 41 | |
Ethanolamine:p-cresol | 1:1 | Stirring at RT for 24 h | Extraction of polysaccharides from Ganoderma lucidum | 42 | |
Diethanolamine:4-chlorophenol | 1:1 | Stirring at RT | Selective separation of aromatic amino acids in water | 43 | |
Ethanolamine:m-cresol | 1:1 | Stirring at RT and drying in a vacuum dryer for 24 h | Flavonoid extraction from waste onion skins | 44 | |
Ethanolamine:4- methoxyphenol | 1:1 | Stirring at RT | Extraction and separation of different polar active phytochemicals from Schisandra chinensis | 45 | |
Choline chloride:levulinic acid + octanoic acid:lauric acid | Severalb | Stirring at RT | Extraction and separation of different of phytochemicals from different botanical sources | 46 | |
Ethanolamine:o-cresol | 1:1 | Stirring at RT | Assessment of pyrethroid pesticides in surface soil samples | 47 | |
Lidocaine:heptanoic acid | 1:1 | Stirring at 60 °C | Determination of bisphenols in beverages | 48 | |
L-Menthol:phenyl salicylate | 1:1 | Stirring at 70 °C | Extraction of polysaccharides from wolfberry | 49 | |
pH | Octylamine:sulfonic acid | 2:1 | Stirring at 80 °C | Extraction of sulfonamides from milk samples | 50 |
Thymol:hexanoic acid | 2:1 | Stirring at 60 °C | Extraction of antibiotics from environmental water samples | 51 | |
L-Menthol:(1S)-(+)-camphor-10-sulfonic acid | 5:1 | Stirring at 40 °C for 20 min | Liquid–liquid extraction of abamectin and endosulfan from water and juice samples | 52 | |
Caprylic acid:capric acid | 3:1 | Stirring at 50 °C | Recovery of β-carotene from pumpkin | 29 | |
Diethanolamine:hexanoic acid | 1:1 | Stirring at 80 °C | Pre-concentration of liposoluble constituents in Salvia miltiorrhiza | 53 | |
Octanoic acid:linalool | 1:1 | Stirring at 80 °C | Extraction of polyphenols from millet | 54 | |
Thymol:octanol | 2:1 | Stirring at 40 °C for 20 min | Analysis of herbicides in water and fruit juice samples | 55, 56 | |
Menthol:n-octanoic acid | 1:2 | Stirring at 80 °C for 1 h | Preparation of pH-responsive nanoemulsions | 57 | |
Dodecaonic acid:octanoic acid | 1:1 | Stirring at 40 °C | Extraction of polysaccharides from grape seeds by three-phase-partitioning | 56 | |
[N4,4,4,4]Br:Triton X | 1:1 | Stirring at 80 °C | Fermentation and purification of fibrinolytic protease from Bacillus subtilis | 58 | |
DL-Menthol:4-aminophenol | 1:2 | Stirring at 60 °C | Extraction of pyrethroid pesticides from milk | 59 | |
DL-Menthol:lauric acid | 1:1 | Stirring at RT | Determination of phthalate esters in the packed milk samples | 60 | |
Ethyl maltol:octanoic acid | 1:2.5 | Stirring at 60 °C | Extraction of oily waste from oily sawdust | 61 | |
Octylamine:succinic acid | 2:1 | Stirring at RT | Extraction and determination of curcumin in water and food samples | 62 |
In order to scientifically demonstrate the transformation of RDES during use and the change in behavior, HBA, HBD and prepared RDES need to be characterized. The characterization of RDES involves various analytical techniques to monitor these changes. Nuclear magnetic resonance (NMR) is widely used to monitor chemical shifts and confirm structural changes in the solvent. Fourier-transform infrared spectroscopy (FTIR) provides information on the changes in hydrogen bonding and molecular interactions.35,63 High-performance liquid chromatography (HPLC) is often used in the characterization of RDES to analyze the composition, purity, and stability of components in RDES, particularly in applications where these solvents are used for extraction and/or separation of target compounds.64,65 Additionally, techniques such as differential scanning calorimetry (DSC) and thermogravimetric analysis (TGA) are employed to evaluate thermal properties of the solvent.66,67 These characterization methods are critical to understanding the dynamics of RDES and optimizing them for specific applications.
The possibility of preparing a DES that responds to CO2 in the medium and changes its physicochemical properties accordingly was first discovered by Sed and co-workers.28 In their study, a hydrophobic fatty acid-based NaDES was mixed with an amine solution and a hydrophilic homogeneous solution was formed by the formation of complexes between the two components. After CO2 was introduced to the solution, the fatty acid anions were reprotonated, restoring the hydrophobicity of the NaDES and causing the two phases to separate. Wan et al.68 prepared a series of CO2-RDES by combining alkanoamine compounds and phenols, resulting in hydrophilic DES that were stirred in a homogeneous solution with water. The addition of CO2 led to a shift in the acidity of the medium, resulting in the formation of an ammonium salt in the aqueous solution and the disruption of the hydrogen bonds between the HBA and HBD, promoting the phase separation, which was evident in the FTIR and 13C-NMR spectra. After the addition of N2, a shift back to the original monophasic state was observed, indicating the complete reversibility of the system. In another study, a switchable DES was prepared from alkanoamines and phenols for the extraction and preconcentration of chlorobenzenes.32 Purging CO2 led to a change in the nanostructure of the DES, resulting in the formation of two separate phases in the reaction mixture. Imidazole, a typical low-cost nitrogenous base, was also used as the HBA for the preparation of CO2-RDES, while polyols were evaluated as HDBs. The addition of olive oil to the DES resulted in the formation of an emulsion, which separated into two phases upon the addition of CO2 and the emulsion formed again upon the removal of CO2 by the introduction of N2.35
Overall, the use of CO2 as a trigger for switchable solvents, including DES, offers some key advantages, namely wide availability and ease of removal. However, this type of RDES has some shortcomings: most of the HBAs and HBDs used for RDES preparation present some toxicity; the DES network is completely disrupted, and during phase separation, the HBAs and HBDs migrate to different phases; not to mention that this process requires additional equipment for gas flow and its regulation. With regard to CO2 release, it should also be noted that the use of CO2 in this context does not contribute to the mitigation of global warming, as it is not permanently sequestered.
For the design of thermo-RDES, HBAs and HBDs must be selected with knowledge of their behaviour, i.e., whether or not they exhibit phase behaviour and if so, whether they have a lower critical solution temperature (LCST) or upper critical solution temperature (UCST). For this reason, alkanolamines are used as HBAs and phenols as HBDs in thermo-RDES. Mixtures with an LCST are completely miscible with water at low temperatures due to favourable hydrophilic interactions such as hydrogen bonding between the DES components and water as well as within the DES itself. However, as the temperature increases and exceeds the LCST, these hydrogen bonds are disrupted by thermal energy, weakening the hydrophilic interactions, and strengthening the hydrophobic interactions, which leads to aggregation of the solute molecules and phase separation into two distinct phases. LCST behaviour is entropy-driven, with an increase in temperature causing the system to favour phase separation as a result of the prevalence of hydrophobic interactions.72 Although LCST behaviour is well-known, it is less common in thermo-RDES.30 UCST phase behaviour, on the other hand, involves phase separation at low temperatures owing to strong solute–solute interactions, such as hydrogen bonding, within the RDES. As the temperature increases, these interactions weaken, allowing the components to dissolve in the solvent and form a homogeneous, water-miscible phase.72,73 This is illustrated in Fig. 3.
A thermo-RDES with UCST phase behaviour was prepared by mixing various short-chain alkanolamines with phenols.43 After inducing the phase shift by increasing the temperature of the water–DES mixture, authors successfully extracted amino acids from water. FTIR and 13C-NMR were used to observe the binding behaviour within the network and confirm the changes in binding strengths between DES–DES and DES–water upon temperature shifts. Xiong et al.74 also designed UCST-based RDES but used only phenolic compounds, which served as both HBAs and HBDs. The prepared thermo-responsive DES were applied for the extraction of 5-hydroxymethylfurfural from the reaction medium, as its extraction and purification is usually challenging. The use of RDES enabled not only good recovery efficiency but also recycling of the DES without loss of efficiency. Some other studies have reported the formation of thermo-RDES with UCST phase behaviour,42,49,75 showing that the HBDs always contained an aromatic compound, namely o-, m- and/or p-cresol,47 guaiacol45 and methoxyphenol.45 However, these compounds have moderate to high toxicity, including ethanolamine, which is frequently used as HBA.46
Regarding the formation of LCST, Longeras et al.30 reported the first possibility of preparing a thermo-RDES that induces phase separation with the temperature increase. Authors mixed licodaine and oleic acid in different molar ratios and with the addition of different amounts of water and investigated the phase transition behaviour. This was initially done under a light microscope with precise temperature control and later with an FTIR spectrometer connected to a Hyperion microscope to allow more detailed characterization. This was only possible through the careful selection of the HBA and HBD. Lidocaine is an amphiphilic molecule and thus serves as a bridge between hydrophilic and hydrophobic interactions. This property is essential for facilitating the temperature-induced phase transition from a monophasic to a biphasic phase, as required for LCST-based RDES. On the other hand, oleic acid is a hydrophobic compound that can self-assemble when its concentration is above the critical micelle concentration. Therefore, their combination allowed the formation of a DES with temperature-dependent behaviour and confirmed the existence of an LCST with good extraction properties. Since then, these systems have been further explored, involving not only lidocaine, but also tetracaine and procaine76 as well as other carboxylic acids, namely pentanoic, hexanoic, heptanoic, octanoic, nonanoic, decanoic, dodecanoic, tetradecanoic and oleic acids.48,76 However, these HBAs exhibit moderate to high toxicity.46 To overcome this significant aspect, Cai and co-workers46 developed a novel temperature-dependent biphasic DES-based system for the extraction of phytochemicals without the need for amines and/or phenols. The authors prepared and mixed a hydrophilic and a hydrophobic DES, while also adding different amounts of water. The hydrophilic DES was choline chloride:levulinic acid in a molar ratio of 1:2 or 1:3, while the hydrophobic DES was either octanoic acid:lauric acid in a molar ratio of 3:1 or nonanoic acid:decanoic acid:lauric acid in a molar ratio of 3:1:1. They then characterised the DES using thermogravimetric analysis and FTIR spectroscopy and investigated the switchability and phase behaviour of these systems as well as the polarity of the solvent. The RDES consisting of the ternary fatty acid mixture proved to be too hydrophobic, which considerably restricted and even impaired the monophasic region. Nevertheless, the use of the binary fatty acid mixture as a hydrophobic DES enabled the development of a well-functioning biphasic phase diagram. With this study, an efficient and more environmentally friendly option of LCST-based RDES for extraction purposes was presented.
Overall, the operation of thermos-RDES is less complex than that of CO2-based RDES yet both present problems associated with the toxicity of the compounds used for the HBAs and HBDs. Besides, at lower temperatures, the system may be too viscous, which can hinder mass transfer.
Jing et al.57 prepared a hydrophobic pH-RDES from menthol and octanoic acid. The prepared DES was mixed with water, and a surfactant-free microemulsion was formed. The emulsion was responsive due to the compounds used for the DESs preparation and was converted into a nanoemulsion after the addition of HCl. Furthermore, the authors showed that the nanoemulsion reverted back to a microemulsion after the addition of NaOH in response to pH changes. In another study, five hydrophobic pH-RDES were prepared by combining a terpenoid, namely thymol, and fatty acids (heptanoic to decanoic acid).50 All RDES were prepared in situ by changing the acidity of the aqueous solution to induce mixing of the precursors. This was possible due to the characteristics of both precursors, which in an alkaline solution, are present in anionic hydrophilic forms, thus being water soluble at high pH values. By decreasing the pH value of the media, the hydrophilic forms are protonated, and the precursors’ molecular form dominates, inducing a phase separation and formation of DES droplets in the solution. After inducing a shift of pH to acidic environment, the RDES formed a hydrophilic organic phase, which was stable in acidic media. Further studies on the production of efficient pH-RDES were conducted by Salamat and Soylat62 who developed a simple and fast extraction method for microextraction procedures. For this purpose, an RDES composed of octylamine: succinic acid was prepared. The RDES was hydrophilic under neutral conditions and therefore miscible with water. After the addition of NaCl, which led to a change in the aqueous environment to an alkaline state, a heterogeneous solution was formed. This phase shift of the RDES was attributed to the choice of HBAs and HBDs. Short-chain fatty acids, such as succinic acid, have hydrophilic properties. As far as octylamine is concerned, increasing the hydrophobic alkyl portion in the amines increases the molar mass of the amines, which leads to a reduction in their water solubility. When mixed with succinic acid to form a DES, the resulting product is hydrophilic but can become hydrophobic by changing the environment and deprotonating the amine groups. The resulting DES was analysed by 1H NMR spectroscopy for its ability to undergo a phase transition with NaOH and HCl.
The development of pH-controlled RDES systems with highly efficient extraction and separation capabilities offers a promising solution to the challenges associated with current switchable phase transition processes, such as high temperature requirements, high energy consumption and the need for specialised equipment. In contrast to other approaches, this method does not require heating of the extraction mixture or the application of additional energy sources to achieve the switch and can therefore also be used in the extraction of temperature-sensitive analytes.50 Additionally, this type of RDES is associated with lower toxicity due to the use of less hazardous precursors.
Carotenoids, such as β-carotene, lutein, and zeaxanthin, are high-value compounds found in many agricultural products and have positive effects on the human body. β-Carotene is specifically hard to recover due to its properties, namely poor water solubility and sensitivity to light, heat and oxygen and is thus often extracted using hazardous solvents. A significant improvement in β-carotene extraction was achieved using pH-RDES.29 By using a fatty acid-based switchable solvent, high amounts of β-carotene were extracted (90 μg mL−1) from pumpkin and simultaneously separated from the pumpkin extract without the need for additional separation processes and solvents. Similarly to carotenoids, plant polysaccharides exhibit pharmacological properties, such as antioxidant, anti-aging, and anti-tumor, but their recovery is difficult as certain methods and solvents commonly used can impair their biological activity. To overcome the challenging polysaccharide recovery, thermo-RDES have been applied for polysaccharides extraction from Lycium barbarum.41 The extraction was performed at room temperature in the monophasic region and the system was then subjected to temperature to promote the phase separation, namely a hydrophobic DES-rich phase and an aqueous phase containing the polysaccharides. This not only allowed the polysaccharides extraction but also the recycling and reuse of DES for five cycles. The extraction yields of polysaccharides were ∼460 and ∼427 mg g−1 of biomass in the first and fifth cycle, respectively. Simultaneously, the RDES recovery efficiencies were 82.5% and 80.2% of the first and fifth cycle, respectively. Thus, proving an efficient use, recycling, and reusing of this thermo-RDES. Another study also reported high polysaccharides extraction yields from Ganoderma lucidum while using thermo-RDES, but this time using a UCST-based system with ethanolamine and p-cresol composing the RDES.42 Results showed it was possible to recover 88% and 79% of the polysaccharides in the aqueous phase after the first and fifth extraction cycle, respectively. Lastly, the authors added CO2 to the DES-rich phase to promote another phase separation and in this case separate the DES components. The top phase was the HBA salt-rich phase whereas the bottom phase corresponded to the HBD-rich phase. The former was further treated with N2 to recover the HBA in the original state, and the HBD was dried, achieving around 90% recovery of p-cresol. Continuing the polysaccharides extraction, Chen et al.56 prepared a series of pH-RDES that were included in a three-phase partitioning to extract and purify polysaccharides from grape seeds and achieved high extraction yields of up to 98.04 mg g−1 under optimized conditions. This represents an almost complete extraction yield on the first cycle. The RDES was later reused in the study during 25 cycles and led to a small yield decrease of 14% in the last cycle.
Moreover, RDES have also been used for the extraction of phytochemicals from plants. Attempting to extract nine different phytochemicals from Roxa roxburghii, a hydrophobic CO2-RDES was prepared and manipulated through the addition of CO2 and N2 to the system.82 The process of alternating the state of the DES in the aqueous solution enabled simultaneous extraction and enrichment of all nine hydrophilic and hydrophobic phytochemicals from R. roxburghii. At the same time, RDES was recycled during the extraction process, offering a new sustainable approach for phytochemical recovery from plants. In a similar study, researchers aimed to develop both highly efficient as well as environmentally friendly methods for flavonoid extraction from waste onion peels.44 For this purpose, UCST-based thermo-RDES were prepared and applied over the microwave-assisted extraction of quercetin, kaempferol, luteolin and quercetin-3-O-β-D-glucoside. Under the optimized conditions, the total flavonoid yields reached ∼48 mg g−1, which was more efficient than traditional organic solvents. However, in order to obtain crude flavonoid extracts, the authors used the macroporous resin HPD 600, allowing recovery rates of >90% for all of the four extracted flavonoid compounds. A similar observation considering the performance of RDES versus other solvents was reported by Zhang and coworkers.83 A pH-RDES with polarity-switching characteristics, namely N,N-dimethylbenzylamine:octanoic acid (1:2 molar ratio) with 3 wt% β-cyclodextrin and 30 wt% water, outperformed pure DES (without β-cyclodextrin) and ethanol in total flavonoid recovery: ∼158 mg g−1 using RDES in comparison with 135 and 105 mg g−1 using pure DES and 60% ethanol, respectively. However, in this study, a macroporous AB-8 resin had to be used to recover the flavonoids and recycle the solvent. After 5 cycles, the extraction efficiency still remained >90%. Lastly, authors performed the cytotoxicity analysis of the RDES, and the results showed an exceptionally low or even negligible cytotoxicity with the EC50 > 2000 mg L−1. Wang et al.53 used a hydrophilic switchable DES for the pre-concentration of liposoluble constituents from Salvia mitiorrhiza. The RDES (diethanolamine:hexanoic acid, 1:1 molar ratio) was prepared and added to the extractant phase in a homogeneous phase. Then, authors added HCl to switch the DES polarity, the RDES became hydrophobic and immiscible with water, hence leading to a biphasic system. This allowed concentration factors of diterpenoid quinones ranging from 59 to 274, which was considerably better than hexanoic acid alone.
Pochivalov and co-workers50 went one step further in terms of using RDES for downstream processing by using RDES for the determination of antibacterial agents in milk samples. The RDES was prepared in situ from a terpenoid and a carboxylic acid after changing the acidity of the aqueous mixture, thus eliminating the need for additional energy sources and heating normally used for DES preparation. This approach proved successful for the determination of sulfamethazine, sulfamethoxazole, sulfaquinoxaline and sulfadiazine in milk samples, with pre-concentration factors between 22 and 103, which increase with increasing hydrophobicity of the analyte.
To summarise, the application of RDES in downstream processes has shown not only high extraction efficiency and selectivity, but also the possibility of solvent recycling and reuse with minimal performance loss.
Thorough research into the pharmacokinetics and pharmacodynamics of drugs is an important part of drug development. For this purpose, the biological samples must be carefully pre-treated, which is traditionally done with hazardous solvents and time-consuming procedures. In an attempt to find an alternative, more environmentally friendly and faster sample pre-treatment method for post-application drug monitoring, Yang et al.91 focused on establishing a liquid–liquid microextraction (LLME) method based on a CO2-RDES. A switchable DES was prepared using 4-methoxyphenol and monoethanolamine as HBD and HBA, respectively, in a 1:2 molar ratio. After mixing the biological samples with the prepared RDES, LLME was applied to remove proteins and lipids, and the alkaloids in the samples were pre-concentrated simultaneously. The injection of CO2 into the reaction mixture changed the RDES properties and led to the two-phase formation, i.e., an aqueous-rich phase and DES-rich phase containing the target analytes. The results provide a new insight into the biological behaviour of drugs in vivo in a simple, fast, and efficient way and demonstrate the possibility of using RDES in pharmacokinetic and pharmacodynamic studies. Similarly, LLME extraction in combination with a RDES was proposed as a new method for the separation and quantification of an anticancer drug daunorubicin in human plasma samples.65 Authors prepared several pH-RDES, with the most efficient one being composed of L-menthol and (1S)-(+)-camphor-10-sulfonic acid in a 5:1 molar ratio. The results showed that daunorubicin was not found in the blank sample, but it was detected in all four real samples in a concentration ranging between of 58.7–188.3 μg L−1. The results showed that the relative recoveries of daunorubicin in plasma samples were in the range of 91.0–107.8%, with an RSD < 7. This proved to be an efficient and robust technique for drug analysis in biological samples.
At this stage, these studies have shown the potential of using RDES in biomedicine but have also made it clear that their application has so far been limited mainly to analytical purposes.
Pollutants, including chemical waste, household waste, heavy metals, and bioactive compounds, have a negative impact on the environment and human health. Tackling the pollution crisis requires both the detection and elimination of pollutants, and RDES are emerging as a tool for this transformation. A switchable DES consisting of thymol and octanoic acid was assessed for the determination of strobilurin fungicides in water, juice, wine, and vinegar samples.33 The method has shown favourable linearity, precision, detection limit and recovery of fungicides with pH adjustment and manipulation of RDES. Furthermore, the method did not require additional solvents and equipment. Another application of RDES to prevent environmental pollution is the extraction of isopropanol from wastewater.39 Herein, several CO2-RDES were analysed, with monoethanolamine: butanol showing the most efficient recovery of isopropanol due to its hydrogen bonding with butanol. Once the CO2 was purged in the system, the RDES dissociated and resulted in the two-phase separation, with HBA salts forming the top phase and a butanol-rich bottom phase containing isopropanol. In this study, the RDES was not recycled as the butanol/isopropanol mixture can now be directly applied in the preparation of alternative fuels.
The presence of high concentrations of estrogenic hormones in environmental samples can have a negative impact on human health and must therefore be closely monitored. Extraction and pre-concentration are crucial steps for analysing these hormones in the samples, which are usually performed using non-environmentally friendly solvents and techniques. In this sense, Fattahi et al.92 developed a fast, simple, and environmentally friendly pre-treatment method using a pH-RDES. The prepared pH-RDES containing L-menthol and (1S)-(+)-camphor-10-sulfonic acid was manipulated by adding KOH to the solution. After changing the polarity, the RDES became miscible with water and a homogeneous mixture was formed, promoting a better interaction of the RDES and the steroids being extracted. Then, HCl was added to the system, restoring RDES hydrophobic state and promoting again the phase separation. The steroid hormones were concentrated in the RDES-rich phase and were then quantified. The sample analysis showed good linearity, precision, and sensitivity of the method as well as ease of use, which emphasizes the potential of RDES for monitoring environmental samples. Ma and co-workers,51 on the other hand, prepared a few pH-RDES using thymol as the HBA and medium-chain fatty acids as the HBDs. RDES were used as solvent in the liquid–liquid extraction of two antibiotics, namely levofloxacin and ciprofloxacin, that most commonly accumulate in environmental water samples, affect the human body and lead to drug resistance in pathogenic bacteria. The extraction of the target analytes was achieved by changing the medium acidity through the addition of HCl, which led to a change in the polarity of the RDES and its miscibility with water. The method showed high extraction efficiency and good repeatability, making it a promising approach for similar pre-concentration and extraction procedures. Likewise, Lu and coworkers93 utilized fatty acid-based RDES to concentrate/extract UV filters from river, lake, sea, and bathing water samples. To achieve this, a dispersive liquid–liquid microextraction was employed, and a switchable solvent, namely a pH-RDES, served two purposes by acting as a dispersive solvent and an extraction solvent, depending on the pH of the solution and thus the solvent's polarity. The prepared octanoic acid-based RDES extracted all target analytes in a short amount of time (within 9 minutes) and the method exhibited low detection limits coupled with a wide linear range, making it a practical and easy approach for water sample monitoring.
Regarding waste management, an ethyl maltol-fatty acid-based pH-RDES was applied for the oil removal from oily sawdust with a ∼67% oil content.61 The process includes multiple steps to recover the oil from the solid and liquid fractions, as shown in Fig. 5. Considering the liquid fraction, i.e., the oil-RDES fraction, the homogeneous phase was disturbed by the addition of NaOH, which deprotonated the RDES and increased its hydrophilicity, thus forcing the phase separation with an oil-rich top phase and aqueous RDES-rich bottom phase. After collecting the oil phase, acetic acid was added to the system, reprotonating the RDES and returning its hydrophobic character, which in turn promoted a new phase separation. This allowed the recycling and reuse of the RDES for 5 cycles with an efficiency loss of ∼10% from the first cycle (∼86%) to the second, remaining stable in the consequent cycles (∼76%). Additionally, authors also studied heavy metals extraction from the same sample and under the optimal conditions, the RDES showed extraction rates of >60% for all explored heavy metals except iron.
The use of RDES in the field of environmental sustainability is far more advanced than in biomedicine, with most studies focusing on the application of RDES to concentrate and extract contaminants from different types of samples either as a monitoring measure or for remediation purposes.
RDES offer the possibility to change solvent properties such as polarity, viscosity, and solubility in response to external stimuli such as CO2, pH, or temperature. This adaptability makes RDES highly versatile for applications, for instance extraction and separation processes.32,43 Their switchable nature contributes to improved selectivity of target compounds, enabling simultaneous extraction of multiple compounds with different chemical properties and leading to better overall performance. In addition, the general adaptability of RDES simplifies separation processes, enhancing the sustainability of industrial processes by reducing solvent consumption and costs. In this context, recyclability is another important feature of RDES. The tunable properties of RDES mean easy and fast solvent recycling, and as shown in several studies, the recycling process hardly affects the effectiveness of the RDES, especially forthermo- and pH-RDES, which is of great importance for sustainable chemistry.41,94 Moreover, RDES are simply a particular type of DES, so their designer solvent character remains one of the most intriguing and useful properties of these solvents. Thus, a wide range of possible green and biocompatible precursors is available, depending only on the switching mechanism and the target application. This is in line with the principles of green chemistry and points to a promising change in chemistry, but also in other areas where the need for better, more efficient, and environmentally friendly solvents and innovations is constantly growing.88
However, despite their great advantages, RDES also face several challenges. The first obstacle is the complexity of some operations, which can lead to higher costs and require additional equipment. CO2-RDES require additional equipment and regulations for their use, as well as special amines and phenols, which are more expensive HBAs and HBDs. Similarly, thermo-RDES require heating to promote phase switching, and in the case of LCST-based RDES, temperatures can be relatively high. This complexity can also hinder the transition to a larger scale. As the name “responsive” implies, these solvents respond to external stimuli. However, to fine-tune the solvent, external stimuli must be precisely controlled, which can complicate some industrial applications.
As far as the recyclability of RDES is concerned, all studies state that it is easy and possible to recover and recycle DES. However, this is not entirely clear for CO2-RDES, especially since CO2 injection leads to the formation of carbonic acid, which in turn reacts with the HBA and induces the formation of an ammonium salt-rich top phase and an HBD-rich bottom phase. At this stage, the HBA and HBD are in separate phases regardless of the location of the analyte, so a further technique is required to separate the DES precursor and analyte before the two phases can be combined and exposed to the N2 stream to restore the HBA character and thus allow the “regeneration” of the RDES. So far, most studies lack a clear explanation on how the analyte is recovered and on how the RDES is recycled and reused. Often, the authors mention that the analyte has preferentially migrated to one of the phases and present its quantification but continue with the discussion of the N2 flux to induce the monophasic state. When the CO2-RDES is recycled and reused, the authors mentioned the number of cycles performed and the extraction efficiency, but without explaining how this was done. In this sense, readers have considerable difficulty understanding the procedures performed in this type of RDES, so future studies should begin to address this shortcoming. This is not to say that only thermo- and pH-RDES enable DES recycling, but these tend to be much clearer, not to mention that both HBA and HBD remain in the same phase during phase separation, which facilitates the RDES recycling. In addition, some studies have reported the use of resins to separate the target compound from DES, allowing the solvents to be reused.44,83
From the point of view of sustainability and biocompatibility, the current RDES are not as biocompatible as the regular DES, which is due to the choice of HBAs and HBDs. To change their properties in response to a stimulus, RDES require precursors with specific properties, and until now, researchers have focused mainly on these properties rather than on the toxicity of these compounds. This is particularly true for HBAs and HBDs that are used in most CO2- and thermo-RDES and generally exhibit moderate to high toxicity.46 In contrast, pH-RDES tend to use more natural compounds such as thymol, menthol, and fatty acids, which could then be labelled as natural RDES. This large current gap offers room for improvement and should encourage scientists to search for more natural compounds with comparable properties to those needed in CO2- and thermo-RDES. In addition, this would further enhance the possibilities and applications of RDES in the biomedical field.
Finally, up to date and to the best of our knowledge, there is not a single study that assesses the environmental footprint of this type of DES (i.e., RDES) and RDES-based processes, nor has anyone conducted a techno-economic analysis of these processes. This clearly shows that the development, understanding and application of RDES in various fields is still in its infancy, especially when compared to the progress made so far with regular DES. Nevertheless, this review has also highlighted the enormous potential of RDES, particularly in downstream processing and in biomedical and environmental applications.
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