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Review

Aqueous Two-Phase Systems Based on Ionic Liquids and Deep Eutectic Solvents as a Tool for the Recovery of Non-Protein Bioactive Compounds—A Review

by
Filipe Smith Buarque
*,
Gabrielle Victoria Gautério
,
Maria Alice Zarur Coelho
,
Ailton Cesar Lemes
and
Bernardo Dias Ribeiro
Department of Biochemical Engineering, School of Chemistry, Federal University of Rio de Janeiro (UFRJ), Rio de Janeiro 21941-909, Brazil
*
Author to whom correspondence should be addressed.
Submission received: 2 November 2022 / Revised: 29 November 2022 / Accepted: 20 December 2022 / Published: 23 December 2022
(This article belongs to the Section Biological Processes and Systems)

Abstract

:
Aqueous two-phase systems (ATPS) based on ionic liquids (IL) and deep eutectic solvents (DES) are ecofriendly choices and can be used to selectively separate compounds of interest, such as bioactive compounds. Bioactive compounds are nutrients and nonnutrients of animal, plant, and microbial origin that benefit the human body in addition to their classic nutritional properties. They can also be used for technical purposes in food and as active components in the chemical and pharmaceutical industries. Because they are usually present in complex matrices and low concentrations, it is necessary to separate them in order to increase their availability and stability, and ATPS is a highlighted technique for this purpose. This review demonstrates the application of ATPS based on IL and DES as a tool for recovering nonprotein bioactive compounds, considering critical factors, results and the most recent advances in this field. In addition, the review emphasizes the perspectives for expanding the use of nonconventional ATPS in purification systems, which consider the use of molecular modelling to predict experimental conditions, the investigation of diverse compounds in phase-forming systems, the establishment of optimal operational parameters, and the verification of bioactivities after the purification process.

1. Introduction

The global market for bioactive ingredients was estimated to be US $27 billion in 2021 and is estimated to reach approximately US $52 billion in 2027, demonstrating the high demand for bioactive products and compounds, whether of animal, plant, or microbial origin, which are intended for application in the food, beverage, dietary supplement, cosmetic, pharmaceutical, and animal feed sectors [1].
The greater demand for bioactive ingredients is related to the population’s greater awareness about health, the search for more adequate diets [2] and, consequently, the use of components with potential health-improving effects, because indicators for diseases, such as obesity, diabetes, stress, sleep disorders, and high blood pressure demonstrate that a large part of the population are affected by such disorders [3,4].
Among the ingredients used in the search for better physiological conditions are bioactive compounds, which are defined as nutrients and nonnutrients that can produce physiological effects beyond their classic nutritional properties [5]. These include proteins, peptides, minerals, carbohydrates, polyphenols, carotenoids, anthocyanins, vitamins, omega-3 fatty acids, organic acids, phytosterols, and others [6,7,8]. Bioactive compounds can modulate metabolic processes in the body that promote health [9], acting as antioxidants, antimicrobials, and anti-inflammatory and antihypertensive agents. In addition, they have an immune-modulating activity and can reduce damage from cell oxidation and from cardiovascular complications [8].
Bioactive compounds are increasingly being incorporated into food and beverage formulations, increasing their nutritional, sensorial, and technofunctional properties [10,11], in addition to their use in the chemical and pharmaceutical areas, where active ingredients have already been patented by several companies [12]. Bioactive compounds are found in complex matrices with a diversity of compounds that may interfere with their applicability; thus, extraction and purification techniques must be applied to separate the target component from the mixture [2] and to increase the availability and stability of bioactive compounds [13], generating new ingredients or products [14]. As they occur naturally in small amounts in their source matrices [15], isolation procedures and particularly, concentration techniques, also need to be applied.
Among the available separation techniques, aqueous two-phase systems (ATPS) can be used as a tool for the selective separation of target bioactive compounds. The formation of ATPS occurs when two water-soluble compounds are mixed above their critical concentrations, resulting in two immiscible phases. Each phase of the system becomes enriched with one of the compounds giving rise to two aqueous phases of different chemical and physical natures, which propitiates the migration of target compounds into one of the phases [16].
ATPS has the advantage of a high extraction and purification capacity, higher selectivity, and a biocompatible environment [17]. Furthermore, the application of ATPS in bioseparation presents several advantages compared to conventional separation methods, including scale-up potential, simple operation, fast separation, low energy consumption and low cost [18].
Standard ATPS based on polymers and salts are commonly applied in the purification of protein-based molecules [19]. However, there are infinite other possibilities for their use in the separation of nonprotein bioactive compounds, including mainly phenolic compounds [20], alkaloids [21], natural pigments [22] and other components of interest. Options include the use of alternative solvents such as ionic liquids (IL) and deep eutectic solvents (DES), which are a new class of green solvents capable of replacing traditional solvents, thus reducing or eliminating the use or generation of hazardous substances, with a consequential reduction in the environmental impact [23,24,25]. Advances in this field, including the molecular modelling of IL and DES, could facilitate the expansion and development of purification systems through model prediction, especially when it comes to new and poorly studied alternative solvents, thus also contributing to reducing the time and money involved [26].
In this sense, this review aims to demonstrate the application of ATPS based on IL and DES as a tool for the recovery of nonprotein bioactive compounds, considering important factors for the application, the main results and the most recent advances in this field. To the best of our knowledge, this is the first time that a literature review has explored the application of nonconventional ATPS to a wide range of compounds of nonprotein origin.

2. Bioactive Compounds

Bioactive compounds are nutrients and nonnutrients that exhibit variations in their chemical structures and thus a variety of bioactive properties [5]. They can be obtained from different sources in nature, including animal [27], plant [28], and microbial sources [8,29].
Bioactive compounds from plants present polyphenols, tannins, flavonoids, vitamins, minerals, fatty acids, dietary fibers and other important compounds of different chemical classes, such as carboxylic acids, alcohols, terpenoids, aldehydes, ketones, esters, and pigments [30]. Bioactive compounds from animal sources include bioactive peptides, haem iron, cholesterol, hormones such as melatonin and cortisol, polyunsaturated fatty acids such as omega-3, and collagen [31]. In the case of the dairy industry, the main bioactive compounds are principally extracted from whey and colostrum, highlighting the peptides α-casein, lactorphin, and lactoferricin [32,33].
The demand for bioactive compounds for industries and the consuming public has increased in recent times, due to the technological effects on food and the physiological effects they produce on the human body, in addition to their classic nutritional properties. Often, the bioactive compound itself is not capable of promoting bioactivity, but produces or induces metabolite effects, or effects on the host’s gut microbiome, after consumption [34].
Bioactive compounds are constantly associated with several beneficial properties for the human body, including antihyperglycaemic potential [35], antioxidant, antimicrobial, and angiotensin-converting enzyme inhibitory activity [36], immune-modulating activity, the ability to protect the immune system, and reducing of damage from cell oxidation and from cardiovascular complications [8].
In addition, in technological terms, several bioactive compounds can be used in food products, for example, as a coloring agent, in preparing flours, to increase shelf-life, and as natural antioxidants [13]. Additionally, bioactive compounds improve the nutritional and physicochemical properties, such as texture, and increase the volume of bakery products, e.g., by influencing the viscosity of solutions [15], among other associated technological characteristics.
Among the bioactive compounds, there are three major groups, with varying bioactivity and applications, that will be discussed in this review in relation to purification through ATPS based on IL and DES: (1) phenolic compounds, (2) alkaloids, and (3) natural pigments.
(1) Phenolic compounds. Phenolic compounds comprise a vast and important group of bioactive compounds. These molecules originated as a plant defence mechanism and are considered secondary metabolites [37,38,39]. Phenolic compounds are generally produced when the plant is subjected to stress conditions, including pathogen infection, excessive light, low temperatures, nutrient deficiency, and others [40]. In plants, phenolic compounds play a role in accelerating the process of pollination and in coloring for camouflage and defence against herbivores, as well as offering activity against bacteria and fungi [37,38,39]. Within the group of phenolic compounds, we will mainly highlight the simple and complex flavonoids, phenolic acids, and colored anthocyanins, for example [38].
(2) Alkaloids. Alkaloids are also secondary metabolites of plants, housed in different parts of the plant and with differing amounts involving critical biological functions for different species, including the destructive activity of some insect species, storage reservoirs of nitrogen, growth regulators, and substitutes for minerals in plants, for example [41,42]. They are included within the group of nitrogen-containing compounds, which may consist of one or more nitrogen atoms (within the heterocyclic ring) [42], responsible for the alkalinity of these compounds [43], responsible for alkalinity of these compounds [41]. In their pure form, alkaloids are colorless and odorless crystalline solids but can also be yellowish and impart a bitter taste [41]. The group of alkaloids includes molecules such as caffeine, nicotine [44], and capsaicin [45], among others.
(3) Natural pigments. Natural pigments are alternatives to synthetic dyes and offer various promising applications due to their better biodegradability, greater compatibility with the environment and lower adverse health effects [46]. They are applied to compensate for the loss of natural color present in foods, which occurs during industrial processing and storage, to give identity to certain products, to standardize or intensify the color, and to give coloration to original colorless products, among other properties [47,48]. Among the group of natural pigments with potential for application, carotenoids (orange, yellow, and red), chlorophylls (green) and phycobiliproteins (phycoerythrin, red; phycocyanin and allophycocyanin, blue) stand out, having several bioactive properties with a positive impact on products and on human health, in addition to their colorific potential [49].

3. Methods for Obtaining Bioactive Compounds and Bioseparation

In general, bioactive compounds can be obtained as follows: (1) by direct recovery from different biomass in which they are naturally present (e.g., leaves, flowers, fruits, seeds, husks, oilseeds, cereals, mushrooms, and residues from processing plant and animal tissues); (2) by the cultivation of microorganisms (e.g., bacteria, filamentous fungi, yeasts, and microalgae); and (3) through chemical synthesis.
In the first case, the recovery strategy adopted will depend on the intrinsic characteristics of the matrix and the target compound. However, common preparation steps include selection, drying, size reduction, and degreasing. Examples include the collection and selection of leaves [50], drying of seeds to standard humidity [51,52], milling and sieving of plant material [53] and, in some cases, the extraction of fat from oleaginous materials [54]. Afterward, the powder material can be incorporated directly into ATPS, which will act as the target compound’s extraction and recovery process [51,54]. In other cases, the matrix is subjected to a solid-liquid extraction step, and then the extract is applied to different ATPS for further purification [52,55,56,57,58].
Several metabolites of industrial interest (e.g., proteins, enzymes, carbohydrates, lipids, pigments, phenolic compounds, and chemicals, among others) [59,60,61,62,63] can be produced by the most diverse microorganisms, including wild strains [64], genetically modified strains [65], or microbial consortium [63]. The recovery of target biocompounds will depend on their intrinsic characteristics, the place where they are produced (inside the cell or in the extracellular medium), the type of cultivation (solid or submerged state), and the culture medium (synthetic or containing industrial byproducts). Intracellular biocompounds require a cell disruption step to release to the liquid phase [60,61,65]. An extraction step follows solid-state cultivations to obtain the liquid extract containing the biocompounds [66]. Submerged cultures can rely on a subsequent clarification step, such as centrifugation and filtration, to obtain cell-free extracts with a reduced level of culture medium components, especially in processes where industrial byproducts are used as the source of nutrients [63,64,67]. After all these steps, the extracts can be directly applied to ATPS for selective extraction or partial purification of the compound of interest [61,65].
Unlike bioactive compounds produced by chemical synthesis, extracts from biomass or cultivation processes are complex, containing other compounds and possible contaminants. For example, microbial cultivations can result in highly diluted extracts containing particulate material and undesirable compounds beyond the bioactive compounds, especially those that use medium-containing industrial byproducts. In this sense, purification steps are applied to obtain purer fractions of the bioactive compound. The choice of purification techniques must consider the ability to maintain the bioactivity of the target compounds, in addition to operational aspects (e.g., process parameters, yield, and scale-up) and the degree of purity required. In addition, the bioactivities of the crude extract and purified target compounds should be evaluated when possible. Some techniques used for purification of the most varied bioactive compounds include precipitation by using salt and organic solvents, membrane separation, and chromatographic approaches [68,69]. In this review, we will focus on extracting bioactive compounds from ATPS based on IL and DES as a tool for recovery, due to its operational advantages, as shown below.

4. Aqueous Two-Phase Systems (ATPS)

ATPS are liquid–liquid extraction processes that have an interesting approach for the extraction of biomolecules requiring a high-water content in the coexisting phases. The advantages of this system are related to the high extraction and purification capacity, higher selectivity, and biocompatible environment [17].
In 1896, Beijerinck observed the formation of two liquid phases after mixing aqueous solutions of gelatine and agar. In order to verify a possible generality of the phase separation phenomenon in systems containing macromolecules, in 1947, Dobry and Boyer–Kawenoki, studied the miscibility of water-soluble polymer pairs in organic solvents and the occurrence of phase separation [70]. However, it was only with the work of Albertsson [71] that the great potential of this system for separating macromolecules, such as proteins, became evident to the scientific community.
ATPS for application in bioseparation present several advantages compared to conventional separation methods. These include simple operation, fast separation, high selectivity, low energy consumption, and low cost [72]. The extremely low interfacial tension of this system (between 0.0001 and 0.1 dina/cm) creates a high interfacial contact area of the dispersed phases, increasing mass transfer efficiency [73,74,75]. These systems have considerable potential for application with excellent technical and economic advantages in downstream processes. In addition, they exhibit several advantages, such as simplicity, rapid separation, efficiency, economy, flexibility, and biocompatibility [75]. The variety of chemical species forming ATPS allows combinations to give rise to systems with diverse physicochemical characteristics, enabling the separation of different analytes [76].
The formation of ATPS occurs when two water-soluble compounds are mixed above their critical concentrations, resulting in two immiscible phases (top phase and bottom phase). Each phase of the system becomes enriched with one of the compounds giving rise to two aqueous phases of different chemical and physical natures, which propitiates the migration of target compounds into one of the phases [16].
The formation of the two phases can be explained as a function of the enthalpy of hydration and the system’s entropy. Although both components have an affinity for water, their hydration enthalpies are different from each other, making it possible for two different thermodynamic scenarios to exist. If the system’s energy is greater than the difference between the enthalpy of hydration and the entropy of the system components, they can coexist in a single phase. However, if the system’s energy is lower, the separation of the constituents becomes favorable, and the two phases are formed in equilibrium [77]. Thus, the separation of phases in ATPS results from each component’s ability to form hydration complexes with the water of the system. This process is influenced by numerous variables, such as the concentration, type and molar mass of the polymer and salt, the pH and the temperature of the system [78,79]. The interactions between the system-forming components command its formation and will be responsible for all the physicochemical properties of the phases at equilibrium [72].
The composition of the system can be represented in a triangular (Figure 1A) or orthogonal (Figure 1B) phase diagram. The orthogonal representation, where the water concentration is omitted (the origin of the orthogonal axis represents pure water), is the most widely used in the literature because it allows the use of any concentration unit, whereas the concentration units are restricted to mass and/or mole fraction in the triangular representation. In both cases, it is possible to identify the solubility curve, also often referred to as the binodal curve or equilibrium curve, separating the monophasic region from the biphasic area. Knowledge of the two-phase area, initial mixing, and composition of the individual phases are crucial for any extraction process design and operation, as well as for understanding the mechanisms that govern the partitioning of a solute between two phases. Phase diagram data are also necessary to develop models that can predict partitioning between phases [80]. For example, in the biphasic region, an initial mixture of composition E results in two coexisting phases with the composition represented by two endpoints, D and F, on the binodal curve.
Binodal curves can be constructed by determining the concentration of the components by different methods. The use of high-performance liquid chromatography is the most accurate method for determining the composition of the phases that form the system [81]. However, the method most widely used, due to its simplicity and speed is based on the titration process between the system’s components. This method is commonly called the cloud-point method. The procedure is performed from the visual observation of the appearance or disappearance of turbidity, which occurs during the titration with another compound, generating experimental points. In general, when the system becomes turbid, there is a change from one to two phases; when changing from two phases to a single phase, the turbidity disappears. System compositions are determined by mass (g) quantification [72]. To correlate the experimental points, different models have been reported in the literature. Tubio, et al. [82] associated the experimental points using an empirical sigmoidal equation (Equation (1)); however, the most proposed model for data correlation is that of Merchuk, et al. [83], which proposed a mathematical model with three adjustable parameters (Equation (2)). We have
[ Y ] = y 0 + a 1 + e ( [ X ] x 0 ) b
Y = A   e x p [ ( B X 0.5 ) ( C X 3 ) ]   ,
where Y and X are the percentages in mass fraction of component 1 and component 2, respectively. The fitting parameters a, b, and x0, and A, B and C are obtained by regressing the data.
Point E refers to the mixing of the components, and points D and F are the compositions in the top and bottom phase, respectively. The connection between these three points forming a well-defined line is called a tie line (TL). Different mixing points along the same tie line always include two phases with the same compositions but different mass-to-volume ratios. The TL are commonly determined by the method of Merchuk, Andrews, and Asenjo [83]. The masses of the mixture components are gravimetrically determined and thoroughly mixed. After equilibrium is reached, the top and bottom phases are separated, and their masses are determined. Each individual TL is determined by applying the lever rule to the relationship between the mass composition of the top phase and the overall system. Once the TL have been determined, Equation (3) through (6) can be solved [83]. We have
Y T = ( Y M   /   α ) ( ( 1 α )   /   α )   Y F
X T = ( X M   /   α ) ( ( 1 α )   /   α )   X F
Y T = f ( X T )
Y F = f ( X F ) ,
where f(X) is the function representing the binodal, the subscript M, T, and F denote the mixture, top phase, and bottom phase, respectively. The value of α is the ratio of the top mass to the total mass of the mixture.
In Figure 1B, the difference between the compositions of the two coexisting phases is numerically described by the tie line length. Higher values of TL length reflect more significant differences between the composition of the lower and upper phases and are often used to correlate the partitioning of solutes between the two phases. Gutowski, et al. [84] showed that the more hydrophobically rich phase becomes increasingly hydrophobic as the divergence between the two phases increases, i.e., with an increase in the tie line length. This thermodynamic parameter is generally used as the determining variable in partitioning processes. The length of the tie line can be calculated by applying Equation (7) [85],
T L L = ( Δ Y ) 2 + ( Δ X ) 2 ,
where ΔY and ΔX are the concentration differences of component 1 and 2 between the phases, respectively.
Point C on the solubility curve is known as the critical point and represents the mixture at which the composition of the coexisting phases has become equal, and the two-phase system ceases to exist (TLL = 0). The determination of the critical point for ternary systems is estimated by applying Equation (8) [72],
Y = f + g X ,
where Y and X are the compositions of component 1 and 2, respectively. f and g are fitting parameters.
The phase-forming constituents are traditionally formed by aqueous solutions of two polymers (e.g., dextran, maltodextrin, polyethylene glycol-PEG) [86,87] or polymer + salt (e.g., PEG and phosphate-, sulphate- or citrate-based salts) [88,89,90]. Despite these systems having been extensively applied to partition different biomolecules, they present high viscosity, which hinders mass transfer and a limited polarity range between the two phases [17,91].
To improve the characteristics of the systems and increase the extraction efficiency of several biomolecules, other less traditional phase-forming constituents, such as organic solvents [92,93,94], IL [84,95], and DES [96,97] have been reported in the literature.

4.1. ATPS Phase-Forming Components

4.1.1. Ionic Liquid (IL)-Based ATPS

In 2003, Gutowski, Broker, Willauer, Huddleston, Swatloski, Holbrey, and Rogers [84] were the first to show that a mixture of an aqueous solution of 1-butyl-3-methylimidazolium chloride ([C4mim]Cl) and K3PO4 could form ATPS with an IL-rich (top) phase and a salt-rich (bottom) phase. This system has additional advantages over polymer-based ATPS, such as low viscosity, fast phase separation, high-extraction efficiencies, and high selectivity, contributing to more cost-effective processes if the proper IL are chosen. IL are ionic compounds belonging to the group of molten salts and are composed of organic cations and inorganic or organic anions, which melt at temperatures below 100 °C [98]. The low melting temperatures of IL are typically associated with the lack of an ordered crystalline structure resulting from weak intermolecular interactions derived from the large size ions and their charge distribution [99]. The ionic nature of IL is responsible for some unique properties: negligible vapor pressure under atmospheric conditions, low flammability, high thermal and chemical stability, enhanced selectivity, high ionic conductivity, and a strong solvation capacity for organic and inorganic compounds [100].
IL can be classified into two main categories: aprotic ionic liquids (AIL) and protic ionic liquids (PIL), which are based on proton donation [101]. AIL forms hydrogen bonds and are IL, consisting mainly of organic cations based on imidazolium, pyridinium, ammonium, and phosphonium. They have high synthesis cost, which hinders their industrial application [102]. PIL are readily synthesized by using an equimolar ratio of a Brønsted acid and a Brønsted base, via proton transfer, and have a highly mobile proton. These reagents (acid and base) are low in cost, and the synthesis is straightforward; thus, PIL are more economical than their aprotic analogues. In addition, AIL can usually be recovered and reused by distillation [103,104]. Some examples of cations and anions can be seen in Figure 2. The term “design solvents” has been used to describe one of the essential advantages of IL: the fact that their physicochemical properties can be tailored by manipulating the chemical structure of their ions and it is therefore able to synthesize an IL for a specific application [105]. Therefore, IL cover the entire range of hydrophilicity and hydrophobicity by tunability. Their adaptability is extendable to IL-based ATPS, supporting the great interest in this type of system in recent years.
IL-based ATPS can be formed when salts, amino acids, carbohydrates, or polymers, are added to an aqueous IL solution [84,106,107,108]. The ability of these compounds to induce ATPS formation depends on their nature. To find these trends, some authors have studied the abilities of different IL to induce phase separation by evaluating their cationic and anionic nature, as well as the length of the alkyl chain.
In general, the formation mechanism in IL-based ATPS (except for systems composed of polymers and IL) is dominated by a salting-out effect on the IL. In these ATPS, the solvent is excluded from an IL-rich phase due to the preferential hydration of the second phase-forming component, which acts as a salting-out species. Thus, the greater the ability to form hydration complexes, the greater the ability to induce phase separation [17,84,106,107].
The effect of the chemical structure of the IL shows a behavior in opposition to that of the salting-out inducing species, i.e., the lower its hydrogen bonding capacity with water, the higher its ability to induce the formation of the system [109]. The influence of the cationic alkyl chain length was extensively studied by evaluating the trends observed in the literature, such as the increased hydrophobicity of the IL (decreased water solubility with increasing alkyl chain length) and the ability of IL with chains longer than hexyl to self-aggregate in aqueous solution. As the alkyl chain length of the cation increases, the ability of the IL to induce ATPS formation also increases. However, when this self-aggregation occurs (chains longer than C6), a change is this trend observed, and the ability to form ATPS is reduced [17,110,111]. Regarding the effect of anions, several works [109,112,113] have suggested that the anionic ability to form ATPS correlates inversely with its hydrogen bond acceptor nature, i.e., the greater its ability to interact with water by hydrogen bonds, the lower its ability to separate phases in aqueous media.
ATPS formed by a polymer and an IL seem to result from more complex mechanisms. Specific interactions are established not only with water but also between these constituents, influencing the salting-in and salting-out effects. Freire, Pereira, Francisco, Rodríguez, Rebelo, Rogers, and Coutinho [108] and Pereira, et al. [114] reported that the ability to form systems increases as the immiscibility between IL and polymer increases. The miscibility between the polymer-IL can be adjusted to influence ATPS formation by changing the nature of the phase-forming components. It has been shown that the effect of the anion is directly related to its ability to be solvated by water. If IL are composed of anions with high hydrogen bond basicity, adding water to the polymer-IL blends will destroy the hydrogen bonds between these constituents and, consequently, ATPS formation. However, the influence of the cation is more complex, and the specific interactions (electrostatic and/or hydrophobic) that can affect the solubility of the compounds also need to be taken into account [108,114].
Several works have been published reporting the application of IL-based ATPS in the extraction of various compounds, identifying alkaloids (caffeine, theobromine, and theophylline) [101], drugs (amoxicillin, ampicillin, diclofenac, naproxen, ketoprofen, ibuprofen, and hormones) [115,116,117,118], proteins (albumin, trypsin, cytochrome, and bovine serum albumin) [119,120], enzymes [88,121], metals (Cr (IV), Cr (III) and Cd2+) [122,123], and phenolic compounds [124,125].
One of the advantages of ATPS is their ability to integrate processes. These systems have been applied to improve partitioning, either by the difference in hydrophobicity or by the polarity of the compounds. In addition to the application of IL as the main constituents of ATPS, the use of small amounts in polymer-based ATPS as adjuvants (5 wt% of the total mass of the system) appears to be an alternative system due to the adaptability of IL to cover a more comprehensive hydrophilic–hydrophobic range. Moreover, these systems overcome the high concentrations of IL in the ATPS, making this technique less expensive and more sustainable.
Some studies have reported that IL can be used as an adjuvant. Pereira, et al. [126] were the first to propose using IL as an adjuvant in a conventional ATPS composed of PEG and salt to separate L-tryptophan. The results indicated that the use of IL as an adjuvant showed modifications in the polarities of both phases, leading to better phase separations. Regarding amino acid partitioning, the adjuvant was found to increase typical solute–solvent interactions (van der Waals forces, electrostatic interactions, hydrogen bonds, and π-π-type interactions) and L-tryptophan migrated preferentially to the PEG-rich phase. These results proved that IL as adjuvants could modify the characteristics of the polymer phase representing an alternative to the limitations of PEG/salt-based ATPS. Souza, et al. [127] studied IL as an adjuvant in an ATPS composed of polymer + salt to increase the biphasic region, and Yang, et al. [128] evaluated the use of IL as adjuvants in polymer + salt ATPS to modify the system’s polarity. Almeida, et al. [129] proposed a system of PEG 200, 300, 400, and 600, sodium sulphate, water, and IL-based adjuvants (imidazolium, piperidinium, and pyrrolidinium at concentrations of 5 or 10%) in the extraction of gallic, vanillic, and syringic acids. The authors reported that all investigated antioxidants preferred the PEG-rich phase and that the adjuvants played a role in adjusting the polarity of the preferred phase.
More recently, an alternative that has been explored is the use of mixtures of IL, which can further increase the range of properties of these compounds and allow properties to be fine tuned. This alternative allows improved flexibility in using these solvents without needing to change their chemical structure, thus avoiding the need to synthesize new compounds [130,131,132].

4.1.2. Deep Eutetic Solvent (DES)-Based ATPS

DES are an emerging class of solvents introduced by Abbott, et al. [133] and are formed from an association of two compounds with a high capacity to form hydrogen bonds (hydrogen bond acceptor (HBA) and hydrogen bond donor (HBD)). The mixture of these compounds gives rise to a decrease in the entropy associated with phase transitions and, consequently, to a significant reduction in the melting temperature of the mixture compared to the melting temperatures of the two separate constituents [134].
DES are simple and fast to prepare (simple mixture of the starting compounds at a given temperature) [135]. Moreover, the starting compounds of a DES are usually of low cost, biocompatible, biodegradable, and, in many cases, derived from renewable resources, allowing development applications with a low cost and reduced environmental impact [136,137]. The combination of different HBDs and HBAs capable of originating eutectic mixtures are numerous. DES have different chemical properties to conventional IL, but have similar physical properties, namely their potential as designer solvents, and are even more flexible. Because no reaction occurs between the HBD:HBA, it is possible to obtain DES in a wide range of relative molar compositions, typically by using ratios of 1:2, 1:1, and 2:1 [137].
Choi and coauthors introduced natural deep eutectic solvents (NADES), where only natural, nontoxic compounds are used (such as organic acids, amino acids, or sugars) [138]. The scientific community has widely accepted NADES because they are the ideal green solvent, with 100% atomic efficiency, prepared from renewable, nontoxic, biocompatible, biodegradable, and inexpensive compounds. Because they are present in cells, NADES are related to health applications, such as in the pharmaceutical, cosmetic, and food industries. Some studies have aimed to extract phenolic compounds from coproducts [139,140,141], there are various studies on the use of NADES/DES to extract phenolic compounds from coffee seeds [142], rosemary [143], grapefruit peel [144], and mulberry leaves [145].
Zeng, et al. [146] were the first authors to propose the application of DES in ATPS. In this work, the applicability of DES is due to their similarity with IL, which can be advantageous due to the relatively simple process of obtaining these solvents. Thus, these solvents were described as being able to form ATPS when combined with the inorganic salt K2HPO4. The authors believe that the phase formation of DES-salt systems is directly linked to the affinity of DES with water, i.e., the lower this affinity, the lower the amount of salt required to obtain the ATPS. Thus, the authors suggest that, there is a competition in these system between DES and salt for the water of the system, where the salt has a high affinity for the water of the system resulting in a phase rich in DES and another phase rich in salt and water.
Pang, Sha, Chao, Chen, Han, Zhu, Li, and Zhang [96] evaluated the use of PEG polymer in the synthesis of DES to be applied in ATPS. DES composed of PEG 2000 and choline chloride showed the ability to form phases with different sodium salts. The DES-Na2CO3 system was chosen for the separation processes. The authors related that the evaluated systems did not result in any type of degeneration of the biomolecules target due to the characteristics of the chosen DES, i.e., acting as a biodegradable solvent.
The literature presented here mainly shows the potential application of DES-based ATPS in the extraction of biomolecules. However, in the cited works, no reference was made regarding the stability of DES applied in ATPS. The high-water content in these systems should be considered, as it can weaken or even break the hydrogen bonds forming the DES [138]. In this context, Passos, Tavares, Ferreira, Freire, and Coutinho [97] reported the stability of DES (choline chloride + organic acids) when applied to ATPS composed of PPG 400. The authors used the nuclear magnetic resonance (1H NMR) technique to evaluate the distribution of DES-forming compounds among the phases. It was found that the initial stoichiometry between the HBA and HBD molecules of the DES did not hold in the phases of the systems. Thus, the hydrogen donor molecules (organic acids) were preferentially partitioned to the PPG-rich phase, whereas the hydrogen receptor was partitioned preferentially to the other phase. In these systems, the phase separation was governed by the salting-out effect of the quaternary ammonium salt on the polymer. The authors further reported that DES-based ATPS are, in reality, quaternary systems [97].
Coutinho and collaborators (2018) clarified that the definition of DES could not be generalized because these are not new compounds or pseudopure compounds, but rather that these should be considered mixtures, avoiding any mistaken purposes. These authors also reinforce that the characteristics conferred to DES (green solvents, economical, and easy to obtain) depend on the compounds used to get them [147].

4.1.3. Organic Solvent-Based ATPS

Organic solvents have great potential in the isolation of target compounds, presenting favorable solubility for the extraction of the matrix sample due to their various properties, such as temperature range, vapor pressure, density, viscosity, surface tension, and chemical and thermal stability. To classify a solvent, the solute–solvent interactions, polarity, and solvent effect are confirmed through spectroscopic, kinetic, or equilibrium measurements [148]. The critical criteria to consider when choosing a solvent as an extraction agent are the solubility of the target compound to be extracted, the affinity toward the solute, and the ease of phase separation [149].
Aqueous solutions of organic solvents and inorganic salts are immiscible at specific concentrations and will form two liquid phases. They are lower in cost than traditional systems formed by polymer–polymer and polymer–salt, are simple to operate, easy to remove from the extracts obtained, easy to scale up, and have low viscosity, rapid phase separation, low toxicity, little interference with analytes, low interfacial tension, and high yield [150].
Salts are used in two-phase aqueous systems due to their salting-out effect, because the addition of electrolytes causes a decrease in the aqueous solubility of organic solvents, such as ethanol, propanol, acetonitrile, tetrahydrofuran, and acetone, among others. Thus, the difference in the acting forces between the ion–water and alcohol–water pairs leads to alcohol exclusion or salt crystallization [19].
Organic solvents have been used as phase-forming components of ATPS, for example, acetone + inorganic salt [151], acetone + potassium salts [152], acetone + PIL [153], acetonitrile + carbohydrates [154], acetonitrile + polyols [155], acetonitrile + polyvinylpyrrolidone (PVP) [124], acetonitrile + IL [101,156], acetonitrile + maltodextrin [157], tetrahydrofuran + salt [93], and tetrahydrofuran + carbohydrates [92,95]. Alcohols have also been reported in the literature as a constituent of ATPS, such as in the study by Ooi, et al. [158] who evaluated the ability of ethanol to induce phase formation with ammonium sulphate, sodium phosphate, and sodium citrate. Reis, et al. [159] reported systems formed by ethanol with potassium salts, and Lo, et al. [160] studied the formation of ATPS composed of ethanol + citrate salts. Farias, et al. [161] evaluated the formation of systems based on ethanol + phosphate salts, carbonate, and citrate + IL (adjuvant), and Chong and Brooks [162] reported the effect of ethanol and propanol as phase-forming components in alcohol–carbohydrate systems.
Several works in the literature have applied organic solvent-based ATPS in the partitioning/extraction/purification of various target biomolecules. Ran, et al. [163] reported the formation of ATPS composed of ethanol/(NH4)2SO4 by using IL [C6mim]BF4 as an adjuvant, evaluating the recovery of proanthocyanins which are antioxidants present in seeds by varying the concentration of the phase-forming components. The extraction efficiency and partition coefficient were observed with increasing organic solvent and salt. Both salting-out effects were the major driving force for the enrichment of solutes in the ethanol-rich phase (top phase), because increasing the salt concentration favored the recovery of proanthocyanins in the organic solvent. Nainegali, et al. [164] studied the ATPS formed by 1-propanol/(NH4)2SO4 in the partitioning of bioactive compounds (anthocyanins, garcinol, isogarcinol, and hydroxy citric acid) from Garcinia indica peels. The authors identified that hydrophobic biomolecules (garcinol and isogarcinol) were partitioned to the alcohol-rich phase. In contrast, hydrophilic biomolecules (anthocyanins and hydroxy citric acid) migrated preferentially to the salt-rich phase. This behavior is due to the hydrophobic interactions and hydrogen bonds between the biomolecules and the salting-out effect of the system.
Regarding the effect of temperature on alcohol-based ATPS, Han, et al. [165] studied systems formed by 1-propanol, 2-propanol, and ethanol + sodium hydroxide and water at different temperatures (283.15 K, 298.15 K, and 303.15 K). The authors observed that the increase in temperature led to the expansion of the two-phase region and the ability to form phases following the order 1-propanol > 2-propanol > ethanol. In this study, the authors also compared the formation aspects of alcohol-NaOH and alcohol–salt systems, where they reported that phase separation may be related to the ionic charge of NaOH (±1) being lower than the ATPS-forming inorganic salts, which have the charge ±2 and ±3. Some authors, such as Hu, et al. [166] and Wang, et al. [167], observed no significant difference in the effect of temperature on the two-phase region of alcohol–salt-based ATPSs. However, for the 1-propanol/2-propanol/2-butanol + diammonium hydrogen citrate system [168] and the 1-propanol/2-propanol/2-methyl-2-propanol/2-butanol + dipotassium oxalate system [169] the effect of temperature on the binodal curve showed that the phase separation ability of these ATPS increased when the temperature was increased. Similarly, Robles, et al. [170] studied the effect of temperature on the system formed by water + ethyl acetate + ethanol at four different temperatures (293.15 K, 298.15 K, 303.15 K, and 308.15 K) and found that there was an increase in the immiscibility region at the lowest evaluated temperatures of 293.15 K and 298.15 K.
The effect of pH has also been described in the literature as a variable that affects the liquid surface charge of the medium. It can be adjusted by aiming at the partitioning of the target compound [115]. Nainegali, et al. [171] studied ATPS formed by alcohols and ammonium sulphate and observed that pH 6 favored the system’s selectivity, where hydrophobic biomolecules were partitioned to the top phase and hydrophilic biomolecules migrated to the bottom phase.
A system derived from ethanol-based ATPS was reported by Buarque, Soares, de Souza, Pereira, and Lima [94] and Buarque, et al. [172]. The authors reported developing a new type of system, the ethanolic two-phase system (ETPS), based on the same principles as traditional ATPS, where water is replaced by ethanol. Thus, ETPS was reported to overcome the main limitation of ATPS, the extraction and purification of highly hydrophobic biocompounds (null water-soluble). The systems were formed by polypropylene glycol 2000 (PPG 2000) + mono-, di-, tri-ethylene glycol + ethanol, showing promising results with remarkable extraction values and selectivity of bixin (hydrophobic model biomolecule) and ascorbic acid (hydrophilic model biomolecule). In the other work, the systems were formed by using PPG of different molecular weights (425, 725, 1000, 2000 g mol−1) + ethylene glycol + ethanol, PPG + IL based on imidazolium + ethanol and PPG + ethylene glycol + IL (as adjuvant) + ethanol (quaternary system). These systems were used to partition curcumin and caffeic acid from saffron (Crocus sativus L.). In the system composed of PPG 2000 and ethylene glycol, a selectivity was observed in which the biomolecules were partitioned to opposite phases with a maximum extraction efficiency of 90.3% for curcumin and 89.1% for caffeic acid. In systems using IL as a constituent or adjuvant, the interactions between the IL and the biocompounds propitiate the migration of curcumin and caffeic acid to the same phase, interfering with the selectivity of the systems. However, the IL-based ETPS showed a complete partition of curcumin (EE = 100%), and caffeic acid reached an EE value of 98.0% for longer alkyl chain IL ([C6min]Cl).

5. Computational Modelling Related to ATPS and Applied to Bioactive Compounds

Because the driving forces in the process of separation and purification of biocompounds are multimodal in nature, and knowing that process optimization is usually done empirically, fundamental knowledge at the molecular level has become a challenging task for research groups. Screening efforts can be reduced by applying design of experiment (DoE) techniques. Klamt and Eckert [173] proposed a new prediction method for the thermodynamic equilibria of fluids and liquid mixtures, named the conductor-like screening model for real solvents (COSMO-RS). This method combines the electrostatic advantages and computational efficiency of the quantum continuous solvation model of the chemical dielectric. COSMO-RS is a method based on unimolecular quantum calculations of the individual species in the system, in which the local deviations of the dielectric behavior and hydrogen bonding are evaluated [174].
In the literature, some studies have reported the application of COSMO-RS as a screening tool for the choice of IL or DES in the process of separation and purification of bioactive compounds. Wojeicchowski, et al. [175] employed COSMO-RS to predict the activity coefficient at infinite dilution and the solubility of phenolic compounds (carnosic acid and carnosol) considering 28 HBA and 49 HBD (1372 possible mixtures). Plácido, Carlos, Galvão, Souza, Soares, Mattedi, Fricks, and Lima [101] reported the use of COSMO-RS in predicting the hydrophobicity, hydrophilicity, and hydrogen bonding data for alkaloids (caffeine, theobromine, and theophylline) and PIL (four cations and three anions) in order to aid in the partition study of these bioactives in PIL- and acetonitrile-based ATPS. Pereira, et al. [176] also reported predictive data by using COSMO-RS for alkaloids (caffeine, theobromine, and theophylline) and IL (choline acetate, [Ch][OAc]) in ATPS formed by PEG + choline-based salts. COSMO-RS has also been used in predicting water activity coefficient values in aqueous IL solutions based on choline [177] and pyridinium, pyrrolidinium, or piperidinium cations (chloride anion in common) [178]. The behavior of IL + water is very important for designing the appropriate phase-forming components in extraction and purification processes.
Other molecular simulation models that have been reported as a viable route to green solvents at the atomic level involve the combination of fixed charge models and preset transferable force fields. This type of model systematically calculates the solvation free energies of a spectrum of solutes with various structural and chemical characteristics in various green solvents. In addition, the ratio of water + ILs or DES and the mass density are also important factors in the application of these solvents in separation and purification processes [26]. Sun, et al. [179] and Sun, et al. [180] performed large-scale molecular simulations of solvation free energies for IL based on a 1-ethyl-3-methylimidazolium cation + dicyanamide, bis(trifluoromethylsulphonyl)imide or trifluoromethylsulphonate [180]; 1-butyl-3-methylimidazolium and 1-hexyl-3-methylimidazolium + bis(trifluoromethylsulphonyl)imide and hexafluorophosphate [179]. The authors mentioned that the solvation thermodynamics were formed by the competition of the electrostatic and dispersive–repulsive contributions to the total solvation free energy. Thus, solvation is actually the average of the behaviors of all solute–solvent pairs in the dataset. The hydration free energy was another calculated parameter, of which it has been stated that the angle = bending potential also introduces nonnegligible errors in some cases. However, the torsional term, which is the most influential part determining the intramolecular conformational preference, agrees quite well with the ab initio calculation.

6. Application of ATPS Based on Ionic Liquids (IL) and Deep Eutectic Solvents (DES) for Bioseparation of Bioactive Compounds

Table 1, Table 2, Table 3, Table 4 and Table 5 present the use of IL, DES, and organic solvents in the construction of systems for separating synthetic or natural compounds from animal, vegetable, and microbial sources, including phenolic compounds, alkaloids, and natural pigments. The ATPS available in the literature prove that it is possible to efficiently, selectively, and sustainably isolate, purify, and concentrate the bioactive compounds in highly complex matrices from the selective partition of the molecules, with high yield [181]. In addition, they demonstrate that it is feasible to reduce the environmental impact caused by the use of volatile solvents in obtaining these compounds [182].
It is important to highlight that studies that contemplate the influence of separation on the maintenance or alteration of bioactivity related to target molecules are not routinely verified, a factor that must be better investigated. Most of the studies were conducted to evaluate the antioxidant activity and pigment recovery [129,183]. However, bioactive compounds can exert multiple biological activities affecting the matrix to which they are added or applied. This potential is almost always ignored, which includes not verifying the activity or maintaining the properties such as antihyperglycaemic [35], antimicrobial, and angiotensin-converting enzyme inhibitory activity [36], immune-modulating activity, the ability to protect the immune system, reducing the damage from cell oxidation, and reducing cardiovascular complications [8].
Table 1. Nonconventional ATPS in the extraction and recovery of phenolic compounds.
Table 1. Nonconventional ATPS in the extraction and recovery of phenolic compounds.
Phenolic
Compounds
Raw MaterialPhase-FormingReference
GeniposideGardenia fruit (Gardenia jasminoides)PE62 (ethylene oxide-propylene oxide, 20:80) copolymer +
Phosphate (KH2PO4, NaH2PO4) and sulfate ((NH4)2SO4, and MgSO4) salts + ethanol (0–10 wt%)
[184]
Salvianolic acid BSalvia miltiorrhizaEthanol or n-propanol + (NH4)2SO4, NaCl, and K2HPO4/NaH2PO4[185]
VanillinSyntheticIL (alkylmethylimidazolium cations, and Cl, Br, dicyanamide, methylsulfate, methanesulfonate, triflate, acetate anions) + K3PO4[186]
AnthocyaninsMulberry (Morus atropurpurea)Ethanol + (NH4)2SO4[187]
Vanillin and L-ascorbic acidsyntheticMethanol, ethanol, 1-propanol and 2-propanol + K3PO4, K2HPO4 and KH2PO4/K2HPO4[159]
Lithospermic acid BSalvia miltiorrhizaEthanol + (NH4)2SO4[188]
Gallic acidSyntheticIL (alkylmethylimidazolium cations, and Cl, Br, dicyanamide, methylsulfate, ethylsulfate, octylsulfate, triflate anions) + Na2SO4, K3PO4, and KH2PO4/K2HPO4[189]
VanillinSyntheticAcetonitrile + carbohydrates (glucose, maltose, galactose, xylose, arabinose, fructose, sucrose and mannose)[154]
VanillinSyntheticAcetonitrile + dextran (6000, 40,000 and 100,000 g·mol−1)[190]
VanillinSyntheticAcetonitrile + polyols (glycerol, erythritol, xylitol, sorbitol and maltitol)[155]
Total phenolics, flavonoids and proanthocyanidinsGrape seeds (Vitis vinifera, cultivar Riesling)Acetone + (NH4)3Citrate[51]
RutinAcerola waste (Malpighia glabra)Methanol, ethanol, 1-propanol and
2-propanol + K3PO4, K2HPO4 and K2HPO4/KH2PO4
[191]
AnthocyaninsGrape juice (Vitis vinifera)Ethanol + NaH2PO4 or (NH4)2SO4[192]
Gallic, vanillic and syringic acidsSyntheticIL (1-butyl-3-methylimidazolium cation, and Br, dicyanamide, methylsulfate, ethylsulfate, triflate anions) + Na2SO4, Na2CO3[193]
Gallic, vanillic and syringic acidsSyntheticPEG 200–600 + Na2SO4 + IL (1-butyl-3-methylimidazolium, 1-butyl-1-methylpiperidinium, 1-butyl-1-methylpyrrolidinium cations, and acetate, thiocyanate, tosylate, Cl, dicyanamide anions)[129]
α-Cyclohexylmandelic acid enantiomersSyntheticIL (alkylmethylimidazolium cation, and dicyanamide, triflate anions) + (NH4)2SO4, Na2SO4, K2HPO4[194]
Secoisolariciresinol diglucosideFlaxseed
(Linum usitatissimum)
IL (alkylmethylimidazolium cation, and dicyanamide, BF4 anions) + (NH4)2SO4[54]
Gallic acidGuava (Psidium guajava)Methanol, ethanol, 1-propanol,
and 2-propanol + K3PO4, K2HPO4 and K2HPO4/KH2PO4
[195]
Eugenol and propyl gallateSyntheticIL (alkylmethylimidazolium, 1-butyl-1-methylpiperidinium, [N4444], 1-butyl-1-methyl-pyrrolidinium cation, and chloride anion) + PEG 1500 or 8000 + K3Citrate/Citric acid or K2HPO4/KH2PO4[196]
Caffeoylquinic acidsLonicera japonica flowersIL (1-butyl-3-methylimidazolium bromide) + K3PO4, K2HPO4, KOH, Na2CO3, [197]
Lignans Schisandra chinensisEthanol + (NH4)2SO4[198]
Lithospermic acid BSalvia miltiorrhizan-butyl alcohol + KH2PO4[199]
Total phenolics, and flavonoidsAronia melanocarpa pomaceEthanol + (NH4)2SO4[200]
Caffeoylquinic acid, parishin, and forsythoside isomers, phyllirin, salidroside, gastrodinSyntheticEthanol/1-Butanol + (NH4)2SO4 and K2HPO4[201]
Hydroxycinnamic acid derivativesCarrots (Daucus carota)Ethanol, n-Butanol or IL ([C2mim]Acetate) + (NH4)2SO4, KH2PO4/K2KPO4[57]
Vanillic acid, vanillin, gallic acid, caffeic acid, syringaldehydeSyntheticPEG 8000 + Sodium Polyacrylate 8000 + Electrolyte (sodium dodecylbenzenesulfonate, sodium dodecylsulfate, [N111 14]Br, [N111 16]Br, C16pyridinium chloride, C16 pyridinium bromide, [C12mim]Cl, [C14mim]Cl)[58]
Chlorogenic acidRamie (Boehmeria nivea)IL (1-butyl-3methylimidazolium cation, and triflate, acetate, propionate, hydrogen sulfate, dihydrogen phosphate anions) + Na2SO4, (NH4)2SO4[202]
AnthocyaninsGrape pomaceIL (1-ethyl-3-methylimidazolium
Acetate) + K3PO4, K2CO3
[56]
Total phenolics, and xylooligosaccharidesWheat chaff (Triticum sp.)Ethanol + (NH4)2SO4[55]
AnthraquinonesRheum officinalisDES (ChCl, [N11110]Br, [N11112]Br, [N111 14]Br, as HBA, and hexafluoroisopropanol as HBD) + (NH4)2SO4, Na2SO4, K2HPO4, Na2HPO4[203]
Phloridzin Crabapple (Malus micromalus)Ethanol + (NH4)2SO4[204]
Chlorogenic acidBlueberry (Vaccinium spp.) leavesDES (ChCl as HBA, and ethylene glycol, glycerol, 1,3-butanediol, citric acid, oxalic acid, sucrose, glucose, maltose as HBD) + K2HPO4[53]
Gallic acidSyntheticDES (ChCl as HBA, and sucrose, glucose, fructose as HBD) + K2HPO4[205]
FlavonoidsSophora japonica flower budsIL (alkylimidazolium cations, and propionate, lactate anions) + K3Citrate[206]
Gallic acid, caffeine, and tryptophanSyntheticDES ([N4444]Cl as HBA, and ethanol, n-propanol as HBD) + K3Citrate/Citric Acid[207]
VanillinSyntheticAcetonitrile + maltodextrins[157]
Total phenolics, and luteinMarigold (Tagetes erecta) flowersEthanol + (NH4)2SO4[208]
Mandelic acid enantiomersSyntheticIL (1-methyl quininium, N,N-dimethyl-L-proline methyl ester, N,N-diethyl-L-proline ethyl ester, N,N,N-trimethyl-L-valinolium cations, and methylsulfate, Br, I anions) + K3PO4, K2HPO4, K2CO3[209]
PsoralenFig (Ficus carica) leavesIL (alkylmethylimidazolium cation, and Br, Cl, nitrate, hydrogensulfate, tetrafluoroborate anions) or Ethanol + Citric acid[210]
Cyanidin-3-O-glucoside, gallic acid and quercetin.SyntheticAcetonitrile + polyvinylpyrrolidone (10,000, 29,000 and 40,000 g·mol−1)[124]
Cyanidin-3-O-glucoside, garcinol, isogarcinol and hydroxycitric acidKokum (Garcinia indica)Ethanol, and 1-propanol + (NH4)2SO4, MgSO4, Na2SO4, ZnSO4, Na3Citrate, NaH2PO4, and K2HPO4[171]
Gallic and protocatechuic acidsSyntheticPEG (400, 1000, 1500, 4000, 6000, 8000, 10,000 and 20,000 g·mol−1) + K3PO4 + acetonitrile[125]
ProanthocyanidinsGrape seedsEthanol + (NH4)2SO4, Na2CO3, and K2HPO4 + IL (alkylmethylimidazolium cation and [TOS], [HSO4], [CH3SO3], [NO3], [Br], [BF4] anions)[163]
PaeonolPaeonia suffruticosa root barkEthanol or Ethyl Acetate + NaH2PO4, (NH4)2SO4, KCl, NaCl, Na2SO4, MgSO4[211]
Rutin and quercetinSyntheticIL (cholinium cation, and alaninate, glycinate, serinate anions) + K2HPO4, K3PO4[20]
Lignin alkaline-IL (alkylmethylimidazolium cations, and Cl anion) + Na2CO3[212]
Kraft ligninEucalyptus globulusPIL (2-Hydroxyethylammonium, bis(2-hydroxyethyl)ammonium, tris(2-hydroxyethyl)ammonium cations, and formate, acetate, propionate, glycolate, lactate anions) + acetone[153]
Total phenolicsPeppermint leaves
(Mentha × piperita) and lemon balm
leaves (Melissa officinalis)
DES (ChCl as HBA, and ethylene glycol, glycerol, glucose, citric acid as HBD) + K2HPO4[213]
LignansSchisandra chinensisEthanol + (NH4)2SO4[67]
Cyanidin-3-O-glucoside, garcinol, isogarcinol and hydroxycitric acidKokum (Garcinia indica) rinds1-propanol + (NH4)2SO4[164]
GenipinGenipap (Genipa americana)IL (monoethanolammonium, di-ethanolammonium, triethanol-ammonium cations, and Cl, dihydrogen citrate, dihydrogen phosphate, hydrogen sulfate, nitrate anions) + Acetonitrile[156]
Total phenolics, flavonoids, and chlorogenic acidHaskap leaves (Lonicera caerulea)Ethanol, 1-Propanol + (NH4)2SO4, NaH2PO4, glucose, and maltose[162]
Vanillin and L-tryptophanSyntheticIL (1-decyl-3-methyl imidazolium chloride) + 2-propanol + K2HPO4[214]
AnthocyaninsGrape pomaceIL (bis(2-hydroxyethyl)ammonium
hydrogen sulfate) + Acetonitrile
[215]
GenipinGenipap (Genipa americana)IL (monoethanolammonium, di-ethanolammonium, triethanol-ammonium cations, and Cl, dihydrogen phosphate, hydrogen sulfate, nitrate anions) + PEG 300–750 or PPG 400[216]
Geniposidic acid and aucubinEucommia ulmoidesIL (alkylmethylimidazolium cations, and Cl, Br, acetate, nitrate, dicyanamide anions) + K2CO3, K2HPO4, (NH4)2SO4[217]
ActeosideCistanche tubulosaIL (alkylmethylimidazolium cations, and Cl, Br, BF4, triflate anions) + NaCl, K2HPO4, NaH2PO4, (NH4)2SO4, Na2SO4, Na3Citrate[218]
Syringic and caffeic acidsSyntheticIL (1-butyl-3-methylimidazolium triflate) + NaCl, K3PO4, K2HPO4, NaH2PO4, Na2SO4, Na2CO3[219]
Vanillic and shikimic acids SyntheticDES (ChCl as HBA, and sucrose, glucose, fructose, xylose as HBD) + n-propanol[220]
FlavonoidsYam (Dioscorea alata) peel.IL (alkyl-(2-hydroxyethyl)-dimethylammonium cations, 4-sulfonatooxy-2,2,6,6-tetramethyl
piperidine-1-yloxyl anion) + K3PO4
[221]
Lignin derivativesSyntheticPEG 8000 + Sodium Polyacrylate 8000 + Electrolyte (NaCl, Na2SO4, IL ([C2mim cation, and Cl, dicyanamide, methanesulfonate, triflate, tosylate anions)[222]
Gallic, ferulic, protocatechuic, caffeic and chlorogenic acids Red apple, yellow pear, purple grape, and native bananaPEG 600 + Na2CO3 + PEG bis (methylimidazolium) ditetrachloroferrate[223]
Syringic acid and eugenolSyntheticDES (betaine as HBA, and xylitol, tartaric acid, glycolic acid, urea as HBD) + t-butanol[224]
Table 2. Nonconventional ATPS in the extraction and recovery of alkaloids.
Table 2. Nonconventional ATPS in the extraction and recovery of alkaloids.
AlkaloidsRaw MaterialPhase-FormingReference
Codeine and papaverineOpium (Pericarpium papaveris)IL (1-butyl-3-methylimidazolium chloride) + K2HPO4[225]
Caffeine, β-carotene, and L-tryptophanSyntheticIL (triisobutyl(methyl)-phosphonium tosylate, tributyl-(methyl)phosphonium methylsulphate and tetrabutyl-phosphonium bromide) + K3PO4[226]
PuerarinPueraria lobataIL (1-carboxymethyl-3-methylimidazolium, 1-hydroxyethyl-3-methylimidazolium and 1-butyl-3-methylimidazolium cations, and Br, Hydroxide, tetrafluoroborate anions) + K2HPO4[227]
Caffeine, nicotine, and xanthineSyntheticIL (alkylmethylimidazolium cations, and Cl, acetate, CH3SO3, HSO4, (CH3)2PO4 anions) + PEG 2000[228]
Caffeine, nicotine, theobromine, and theophyllineSyntheticIL (alkylmethylimidazolium cations, and Cl anion) + K3Citrate/Citric Acid[229]
Caffeine and nicotineSyntheticIL (alkylimidazolium cation, and Cl, triflate, trifluoroacetate, acetate, methanesulfonate anions) + K3PO4[230]
Matrine and oxymatrine Sophora flavescensEthanol + (NH4)2SO4 or K2HPO4[231]
GlaucineGlaucium flavumIL (1-butyl-3-methylimidazolium acesulfamate) + Na2CO3, (NH4)2SO4, MgSO4, NaH2PO4[232]
CaffeineGuaraná seeds (Paullinia cupana), and coffee beans (Coffea canephora, Coffea arabica)Methanol, ethanol, 1-propanol and 2-propanol + K3PO4, K2HPO4 and K2HPO4/KH2PO4[233]
CapsaicinCapsicum frutescens var. malaguetaAcetonitrile + IL (cholinium cation, and Cl, bitartrate, dihydrogen citrate anions)[234]
Monoester- and diester-diterpenoid aconitinesAconitum carmichaeliIL (alkylmethylimidazolium cation, and Br, tetrafluoroborate
anions) + K2HPO4
[235]
CaffeineSyntheticIL ([C4mim]BF4) + Na2SO4, NaNO3[236]
Caffeine, theobromine, and theophyllineSyntheticPEG 600 + IL (cholinium cation, and Cl, acetate, bicarbonate, dihydrogencitrate, dihydrogenphosphate anions)[176]
CapsaicinCapsicum chinense var. cumari-do-Pará.Ethanol + NaH2PO4, Na2S2O3, Na2SO4, and Na2CO3[237]
Capsaicincapsicum oleoresinEthanol + Na2CO3, (NH4)2SO4, NaH2PO4, Na3Citrate[45]
Caffeine, nicotine, gallic acid, vanillic acid, amino acidsSyntheticCholine chloride/Glucose + PPG 400[238]
Caffeine, codeine, and vanillinSyntheticEthanol, 1-propanol, and 2-propanol + carbohydrates (xylose, L-arabinose, glucose, galactose, fructose, sucrose, maltitol, xylitol, and maltose)[239]
Matrine, sophocarpine and oxymatrineSophora tonkinensisEthanol + Na2HPO4, NaH2PO4, and Na3PO4[240]
SinomenineSinomenium acutumEthanol + (NH4)2SO4 + ionic liquids ([C4mim]Br, [C6mim]Br, [C8mim]Br, [C4mim]FeCl3Br, [C2OHmim]FeCl4, [C6mim] FeCl3Br and [C8mim] FeCl3Br)[241]
Caffeine, theobromine, and theophyllineSyntheticPIL (2-hydroxyethylammonium, bis(2-hydroxyethyl) ammonium, N-methyl-2-hydroxyethyl-ammonium cations, and acetate, propionate, butyrate, pentanoate anions) + Acetonitrile[101]
Caffeine, nicotine, gallic acid, vanillic acid, amino acids, β-caroteneSyntheticCholine chloride + alcohols (ethanol, n-propanol, ethylene glycol, 1,2-propanediol) + K2HPO4[242]
Caffeine, nicotine, gallic acid, vanillic acid, amino acids, eugenolSyntheticPEG 400 + IL (1-butyl-3-methylimidazolium, 1-butyl-1-methylpyrrolidinium, 1-butyl-3-methylpiperidinium, tetrabutylammonium, tetrabutylphosphonium cations, and chloride anion) + K3Citrate/Citric Acid[243]
Caffeine and theobromineSyntheticIL (N-methyl-N-alkyl-N,N-di(hydroxyethyl)ammonium cations, and Br anion) + K2CO3, K3Citrate, and K3PO4[244]
Berberine HClRhizoma coptidis (Coptis chinensis, C. deltoidea, or C. teeta)IL (alkyl-(2-hydroxyethyl)-dimethylammonium cations, 4-sulfonatooxy-2,2,6,6-tetramethyl
piperidine-1-yloxyl anion) + K3PO4, K2CO3, Na3Citrate, K3Citrate, K2HPO4
[245]
Caffeine and nicotineSyntheticEthanol + K2CO3, K3Citrate, K2HPO4, NaH2PO4, and K3PO4[246]
Caffeine, nicotine, gallic acid, vanillic acid, amino acids, eugenolSyntheticPEG 400 + IL (1-butyl-3-methylimidazolium, 1-butyl-1-methylpyrrolidinium, 1-butyl-3-methylpiperidinium, tetrabutylammonium, tetrabutylphosphonium, cholinium cations, and chloride anion) + (NH4)2SO4[247]
Codeine and caffeineSyntheticIL (1-butyl-3-methylimidazolium tetrafluoroborate) + sugars (xylose, arabinose, fructose, glucose, maltose, sucrose)[21]
CaffeineSyntheticTetrabutylphosphonium bromide + sorbitol[248]
Caffeine, nicotine, amino acids (L-tryptophan, L-phenylalanine and L-tyrosine) and phenolic compounds (gallic acid and vanillic acid)SyntheticEthanol + [N111(2OH)]Cl + NaH2PO4, K2HPO4, K3PO4, K2CO3, and K3Citrate[161]
Caffeine, nicotine, theobromine, and theophyllineSyntheticPluronic PE6200 + IL(cholinium cation, and Cl, acetate, propionate butanoate, lactate, bitaratrate, dihydrogenphosphate, dihydrogencitrate, bicarbonate anions)[44]
Caffeine, nicotine, amino acids (L-tryptophan, L-phenylalanine and L-tyrosine) and phenolic compounds (gallic acid and vanillic acid)SyntheticZwitterions (4-(triethylammonio)-butane-1-sulfonate, 4-(1-methylimidazolium-3-yl)butane-1-sulfonate, 4-(1-vinylimidazolium-3-yl)butane-1-sulfonate, 4-(1-methylpyrrolidinium-1-yl)butane-1-sulfonate, 4-(1-ethyl-piperidinium-1-yl))butane-1-sulfonate) + K2CO3[249]
CaffeineSyntheticIL (tetrabutylammonium cátion, and amino acids anions) + K3PO4, K2HPO4 and K2CO3[250]
CaffeineSyntheticCholine chloride/saccharose + polyethylene glycol dimethyl ether 250[251]
Table 3. Non-conventional ATPS in the extraction and recovery of natural pigments.
Table 3. Non-conventional ATPS in the extraction and recovery of natural pigments.
PigmentsRaw MaterialPhase-FormingReference
CrocinsCrocus sativus stigmasIL (alkylmethylimidazolium cation, acetate and BF4) or Ethanol + NaH2PO4, K2HPO4/KH2PO4[252]
Chlorophyllsilkworm excrementEthanol + NaOH[253]
CurcuminoidsCurcuma longa powderIL (1,3-Diethylimidazole, 1,3-dioctylimidazole, 1,3-dimethylimidazole, 1,3-dibutylimidazole cations, and Br, I anions) + K2HPO4[254]
BetaninOpuntia ficus-indicaTetrahydrofuran + Na2CO3 and Na3Citrate[255]
C-PhycocyaninSpirulina (Arthrospira platensis)IL (alkylmethylimidazolium cations, and bromide anion) + K2HPO4, K2HPO4, K2CO3[183]
CurcuminsyntheticTetrabutylphosphonium bromide + sorbitol, fructose[256]
AstaxanthinShrimp wasteIL (tetrabutylammonium,tetrabutylphosphonium, tributyloctylphosphonium cations, and Cl, Br anions) + K3PO4[22]
CurcuminCurcuma longa rhizomesPluronic F68/McIlvaine buffer (pH 6.0; K2HPO4/Citric Acid) + IL (cholinium cation, and Cl, acetate, propanoate, butanoate, hexanoate anions)[257]
R-PhycoerythrinPorphyra yezoensisDES (ChCl as HBA, and glycerol, ethylene glycol, sorbitol, urea, glucose, fructose as HBD) + K2HPO4[258]
C-PhycocyaninArthrospira platensisDES (ChCl as HBA, and glycerol, ethylene glycol, urea, glucose, fructose as HBD) + K2HPO4[259]
BetaninBeetroot (Beta vulgaris)Tributylmethylammonium hexanoate + Trioctylmethylammonium adipate[260]
Curcuminsynthetic1-ethylpiperazinium
tetrafluoroborate + sodium dodecyl sulfate, and 1-phenylpiperazinium tetrafluoroborate + sodium dodecyl benzene sulfonate
[261]
CrocinsyntheticDES (ChCl as HBA, and urea, ethylene glycol as HBD) + Acetonitrile[262]
Table 4. Nonconventional ATPS in the extraction and recovery of other plant, marine, and algae metabolites.
Table 4. Nonconventional ATPS in the extraction and recovery of other plant, marine, and algae metabolites.
MetabolitesRaw MaterialPhase-FormingReference
GlycyrrhizinGlycyrrhiza uralensis2-Propanol or ethanol + (NH4)2SO4 or K2HPO4[263]
DNASalmon testesDES ([N4444]Br as HBA, and ethylene glycol, propylene glycol, butylene glycol, n-butanol as HBD) + Na2CO3, K2HPO4, NaH2PO4, Na2SO4[264]
PolysaccharidesGentiana scabraEthanol + NaH2PO4,
K2HPO4, (NH4)2SO4, Na3Citrate, and K2CO3
[50]
GinsenosidesPanax ginsengIL (n-alkyl-tropinium and n-alkylquinolinium bromide) + Na3Citrate, K3Citrate, K2CO3, K3PO4, K2HPO4, and NaH2PO4[52]
Polysaccharides Lilium davidii var. unicolorEthanol + Na2CO3, K2HPO4, (NH4)2SO4, and NaH2PO4[265]
GinsenosidesKang’ai injection (Astragalus membranaceus, Panax ginseng and kushenin)DES (ChCl as HBA, and glycerol, ethylene glycol, 1,4-butanediol, glucose as HBD) + K2HPO4[266]
Carbohydrates, ProteinsNeochloris oleoabundans and Tetraselmis suecica.IoliLyte 221 PG + K3Citrate/Citric Acid[60]
Proteins, Arabinan and glucanIsochrysis galbanaIL (alkylmethylimidazolium cations, and Cl, acetate, triflate, dicyanamide anions) + K3PO4, K2HPO4[267]
DNASalmon testes[N4444]Br/PPG 400 + IL (betainium cation, and formate, acetate, propionate, butyrate anions) or DES (betaine as HBA, and glucose, xylitol, sucrose, sorbitol as HBD), or salts (Na2CO3, K2HPO4, NaH2PO4, Na3Citrate)[268]
PristimerinMortonia greggiiIL (1-ethyl-3-methylimidazolium acetate, 1-butyl-3-methylimidazolium
tetrafluoroborate), or Ethanol + Sodium Phosphates
[269]
Ursolic acidCynomorium songaricumEthanol + DES (ChCl as HBA, and acetamide, glycerol, urea, ZnCl2, mannitol, organic acids as HBD) + K3PO4, (NH4)2SO4, Na2SO4[270]
Ursolic acidCynomorium songaricumDES (ChCl as HBA, and glycerol, ethylene glycol, urea, glucose as HBD) + K2HPO4[271]
GinsenosidesPanax quinquefoliusEthanol + Na2CO3[272]
Ginsenoside CKPanax notoginsengDES (ChCl as HBA, and glycerol, ethylene glycol, urea, glucose as HBD) + K2HPO4[273]
Carbohydrates, proteins, lutein and chlorophyllNeochloris oleoabundansPEG 8000 + Sodium polyacrylate 8000 + electrolyte (sodium dodecyl sulfate, 1-methyl-3-tetradecylimidazolium chloride, tributyl-1-tetradecylphosphonium chloride, 1-dodecyltrimethyl-ammonium bromide)[61]
Carbohydrates, proteins, lutein and chlorophyllNeochloris oleoabundansPPG 400 + IL (cholinium cation, and Cl, dihydrogencitrate, acetate, dihydrogenphosphate, bicarbonate, bitartrate anions)[274]
Starch, glucose, proteinsNeochloris oleoabundansPEG 400 + IL (choline dihydrogen phosphate), and IoliLyte 221 PG + K3Citrate/Citric Acid[275]
α-Tocopherol and β-caroteneTetraselmis suecicaIL (cholinium glycinate, cholinium phenylalaninate, cholinium dipeptide, 1-ethyl-3-methylimidazolium methylsulfate) + K3PO4[276]
DNAFish spermIL (alkylhydroxyammonium, alkylammonium cations, and bromide anion) + K2HPO4/KH2PO4[277]
Lipids, lutein Neochloris oleoabundansPEG 400 + IL (choline dihydrogen phosphate), and IoliLyte 221 PG + K3Citrate/Citric Acid[278]
Table 5. Nonconventional ATPS in the extraction and recovery of microbial bioproducts.
Table 5. Nonconventional ATPS in the extraction and recovery of microbial bioproducts.
BioproductsRaw MaterialPhase-FormingReference
Nucleic acidsEscherichia coli K-12, Saccharomyces cerevisiaeEthanol + KH2PO4[279]
2,3-butanediolKlebsiella pneumoniae CICCEthanol + K2HPO4[280]
2,3-butanediolKlebsiella pneumoniae DSM2026Methanol, ethanol, isopropanol + NaCl, K2CO3, K3PO4, and (NH4)2SO4[281]
1,3-propanediolKlebsiella pneumoniae CGMCC 2028Ethanol + Na2CO3[282]
Red colorantPenicillium purpurogenum DPUA 1275Tetraethylammonium bromide, tetrabutylammonium bromide, and 1-butyl-3-methylimidazolium chloride + citric acid/K3Citrate[62]
Succinic acidActinobacillus succinogenes CGMCC1593Ethanol, Isopropanol, Acetone + K2CO3, K3PO4, K2HPO4, NaH2PO4, (NH4)2SO4[151]
Succinic acidSimulated brothAlcohols (ethanol, 1-propanol, 2-propanol, t-butanol) or IL (alkymethylimidazolium cations, and bromide anion) + K2HPO4, Na3Citrate, Na2SO4[283]
RNAYeastDES ([N4444]Cl, [N2222]Cl, [N4444]Br, [N2222]Br as HBA, and PEG 200–4000 as HBD) + Na2CO3, K2HPO4, NaH2PO4, Na3Citrate, (NH4)2SO4, MgSO4, K3PO4, K2CO3, NaCl, NH4NO3[284]
Rubropunctamine and monascorubramineMonascus anka CICC 50131-butyl-3-methylimidazolium chloride + Triton X-100[285]
sRNAEscherichia coliIL (cholinium cation, and amino acids anions) + PPG 400[286]
EctoineHalomonas salinaIL ([C4mim]BF4) + (NH4)2SO4, Na3Citrate[287]
AcetoinBacillus subtilis CGMCC 13141IL (ethanolammonium, isopropanolammonium cations, and acetate, propionate, butyrate, lactate anions) + K3PO4[67]
ViolaceinYarrowia lipolyticaTween 20 + IL (cholinium cation, Cl, acetate, dihydrogenphosphate, dihydrogencitrate, bicarbonate anions)[65]
RoseoflavinStreptomyces davaonensis1-ethyl-3-methylimidazolium acetate or Ethanol + NaH2PO4/Na2HPO4[59]
ε-PolylysineBacillus licheniformisPPG-400 + IL (2-hydroxyethylammonium, cholinium cations, and formate, acetate anions)[64]
Lactic acidMicrobial consortiumIL (alkylmethylimidazolium cations, and BF4, triflate anions) + glucose, xylose[63]
Although it is essential to understand the mechanism of migration between the phases of the system used, the maintenance of the biological activity of the target molecule is a critical factor for the success of its separation and, mainly, its application in food, chemical, or pharmaceutical products [18].
The diversity of ATPS in the literature demonstrates its versatility, robustness, ease of operation, and reproducibility [18]. Furthermore, the use of APTS for the extraction, purification, and concentration of bioactive compounds is advantageous in not needing to use severe operating conditions (high temperatures and pressures or the need for sophisticated equipment), which contribute to the cost and complexity of the process [182] and even lead to the deactivation of the target molecules, with loss of their bioactivities. Thus, such characteristics make the technique necessary to separate and concentrate bioactive compounds [8,18].

7. Conclusions and Future Perspectives

ATPS-based on IL and DES are ecofriendly choices that can be used as tools for the selective recovery and separation of bioactive compounds. However, due to the complexity of the matrices in which these compounds are found, it is necessary to advance more efficient systems that allow their separation. Investigations of phase-forming, nonconventional ATPS processes should be further explored and optimal operational parameters should be established. Molecular simulation as a prescreening tool is also promising for the expansion of nonconventional ATPS in separating and purifying bioactive compounds. It is also necessary to expand the number and diversity of compounds used in the construction of ATPS, providing greater versatility and wider options for their effective application in the purification of bioactive compounds. The increase, maintenance or loss of the bioactivities of bioactive compounds must be verified after separation by nonconventional ATPS, thus ensuring the viability and functionality of these compounds in their future applications.

Author Contributions

The authors contributed equally to this work. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Data Availability Statement

Not applicable.

Acknowledgments

The authors acknowledge the Coordenação de Aperfeiçoamento de Pessoal de Nível Superior—Brasil (CAPES—Finance Code 001), Conselho Nacional de Desenvolvimento Científico (CNPq) and Fundação Carlos Chagas Filho de Amparo à Pesquisa do Estado do Rio de Janeiro (FAPERJ).

Conflicts of Interest

The authors declare no conflict of interest.

Nomenclature

AIL—Aprotic Ionic Liquid; ATPS—Aqueous Two-phase System; COSMO-RS—Conductor-like Screening Model for Real Solvents; HBA—Hydrogen Bond Acceptor; HBD—Hydrogen Bond Donor; IL—Ionic Liquid; NADES—Natural Deep Eutectic Solvent; PEG—Polyethylene Glycol; PIL—Protic Ionic Liquid; TL—Tie Line.

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Figure 1. Ternary phase diagram for a hypothetical system composed of solute A + solute B + water. (A) triangular phase diagram; (B) orthogonal phase diagram; (C) binodal curve; (D) Composition of solute B-rich phase; (E) Composition of initial mixture; (F) Composition of solute A-rich phase.
Figure 1. Ternary phase diagram for a hypothetical system composed of solute A + solute B + water. (A) triangular phase diagram; (B) orthogonal phase diagram; (C) binodal curve; (D) Composition of solute B-rich phase; (E) Composition of initial mixture; (F) Composition of solute A-rich phase.
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Figure 2. Structures of anions and cations that can be combined to form IL.
Figure 2. Structures of anions and cations that can be combined to form IL.
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Buarque, F.S.; Gautério, G.V.; Coelho, M.A.Z.; Lemes, A.C.; Ribeiro, B.D. Aqueous Two-Phase Systems Based on Ionic Liquids and Deep Eutectic Solvents as a Tool for the Recovery of Non-Protein Bioactive Compounds—A Review. Processes 2023, 11, 31. https://0-doi-org.brum.beds.ac.uk/10.3390/pr11010031

AMA Style

Buarque FS, Gautério GV, Coelho MAZ, Lemes AC, Ribeiro BD. Aqueous Two-Phase Systems Based on Ionic Liquids and Deep Eutectic Solvents as a Tool for the Recovery of Non-Protein Bioactive Compounds—A Review. Processes. 2023; 11(1):31. https://0-doi-org.brum.beds.ac.uk/10.3390/pr11010031

Chicago/Turabian Style

Buarque, Filipe Smith, Gabrielle Victoria Gautério, Maria Alice Zarur Coelho, Ailton Cesar Lemes, and Bernardo Dias Ribeiro. 2023. "Aqueous Two-Phase Systems Based on Ionic Liquids and Deep Eutectic Solvents as a Tool for the Recovery of Non-Protein Bioactive Compounds—A Review" Processes 11, no. 1: 31. https://0-doi-org.brum.beds.ac.uk/10.3390/pr11010031

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