Liquid–liquid extraction is a method to separate compounds based on their relative solubilities in two different immiscible liquids, often water and an appropriate organic solvent. During extraction process, there is a net transfer of one or more components between the two liquid phases. This partitioning of compounds allows for purification of reaction mixtures or transfer of desirable products to an organic phase that is more easily evaporated than water.
Liquid–liquid extraction is a technique used in both chemical laboratories and in industrial separations. Separatory funnels are commonly used for small-scale separations in research or teaching labs.
Liquid-liquid extraction is commonly used for organic compounds in the scent/flavor industry, the pharmaceutical industry, and other chemical industries. Metal ions can also be separated using appropriate chelating agents to favor extraction of certain ions into aqueous vs. organic phases like the PUREX process used to separate uranium from plutonium.
Liquid-Liquid extraction can be substantially accelerated in microfluidic devices, reducing extraction and separation times from minutes/hours to mere seconds compared to conventional extractors.
Measures of effectiveness
Distribution ratio In solvent extraction, a distribution ratio (D) is often quoted as a measure of how well-extracted a species is. The distribution ratio is a measure of the total concentration of a solute in the organic phase divided by its concentration in the aqueous phase. The partition or distribution coefficient (Kd) is the ration of solute concentration in each layer upon reaching equilibrium. This distinction between D and Kd is important. The partition coefficient is a thermodynamic equilibrium constant and has a fixed value for the solute’s partitioning between the two phases. The distribution ratio’s value, however, changes with solution conditions if the relative amounts of A and B change. If we know the solute’s equilibrium reactions within each phase and between the two phases, we can derive an algebraic relationship between Kd and D. The partition coefficient and the distribution ratio are identical if the solute has only one chemical form in each phase; however, if the solute exists in more than one chemical form in either phase, then Kd and D usually have different values. Depending on the system, the distribution ratio can be a function of temperature, the concentration of chemical species in the system, and a large number of other parameters. Note that D is related to the Gibbs Free Energy (ΔG) of the extraction process.
In solvent extraction, two immiscible liquids are shaken together. The more polar solutes dissolve preferentially in the more polar solvent, and the less polar solutes in the less polar solvent. In this experiment, the nonpolar halogens preferentially dissolve in the non-polar mineral oil.
Separation factors The separation factor is one distribution ratio divided by another; it is a measure of the ability of the system to separate two solutes. For instance, if the distribution ratio for nickel (DNi) is 10 and the distribution ratio for silver (DAg) is 100, then the silver/nickel separation factor (SFAg/Ni) is equal to DAg/DNi = SFAg/Ni = 10.
Measures of success Success of liquid–liquid extraction is measured through separation factors and decontamination factors. The best way to understand the success of an extraction column is through the liquid–liquid equilibrium (LLE) data set. The data set can then be converted into a curve to determine the steady state partitioning behavior of the solute between the two phases. The y-axis is the concentration of solute in the extract (solvent) phase, and the x-axis is the concentration of the solute in the raffinate phase. From here, one can determine steps for optimization of the process.
Techniques and equipment
Liquid-liquid extraction is often performed on a small scale by synthetic lab chemists using a separatory funnel, Craig apparatus or membrane-based techniques. On an industrial scale, devices like centrifugal contactors, thin layer extraction, spray columns, pulsed columns, and mixer-settlers are used to aid extraction. All of these techniques aim create a high surface area interface between the two liquid phases involved in extraction to aid the transfer of solutes from one phase to the another.
Batch methods
Separatory funnels Separatory funnels, colloquially called a "sep funnel," are commonly used for small-scale extractions in research or teaching labs. To perform an extraction, two immiscible liquids, typically an aqeuous solution and an organic solvent, are added to the sep funnel. The sep funnel is then shaken using appropriate technique to increase the area of contact between the two phases to aid extraction. After the two layers are allowed to settle and separate, each layer is drained from the bottom of the sep funnel into separate containers. Multiple extractions may be performed on the same reaction mixture to increase product recovery. After extraction, the extract phase can be used for further processing
Partitioning of organic compounds between the organic and aqueous phases can be controlled by adjusting the pH of the aqeuous phase. For example, increasing the pH of the aqueous solution will deprotanate organic acids, giving them a negative charge that favors partitioning into polar solvents like water. Adding a strong acid to decrease pH can have the opposite effect, neutralizing conjugate bases to form neutral compounds that can partition more easily into the organic phase.
This technique can be used in teaching labs to extract compounds like caffeine from coffee or tea using ethyl acetate as the organic extractant.
Dispersive liquid–liquid microextraction (dLLME) Dispersive liquid-liquid microextraction is process used to extract organic compounds from water samples, typically at a smaller scale than LLE using a separatory funnel. In this process, an extraction solvent immiscible with water is mixed with a dispersive solvent. The mixture is injected into the aqueous sample to be extracted, forming a dispersion of small organic droplets in the aqueous sample. The resulting suspension is then centrifuged to coalesce the organic droplets and separate the organic and aqueous layers. The organic phase can then be removed using a microsyringe or other tool.
Chlorinated solvents are commonly used as the extractive solvent as their higher density makes them settle to the bottom of centrifuge tubes. Acetone is a common dispersive solvent.
dLLME is favored for its relatively low use of organic solvent for a batch extraction process which can reduce costs. The lower solvent usage means dLLME can be considered a "green chemistry" process though common use of chlorinated solvents as the organic phase is typically considered antithetical to green chemistry principles.
This process is useful in extraction organic compounds such as organochloride and organophosphorus pesticides, as well as substituted benzene compounds from water samples.
Continuous processes
These are commonly used in industry for the processing of metals such as the lanthanides; because the separation factors between the lanthanides are so small many extraction stages are needed. In the multistage processes, the aqueous raffinate from one extraction unit is fed to the next unit as the aqueous feed, while the organic phase is moved in the opposite direction. Hence, in this way, even if the separation between two metals in each stage is small, the overall system can have a higher decontamination factor.
Multistage countercurrent arrays have been used for the separation of lanthanides. For the design of a good process, the distribution ratio should be not too high (>100) or too low (<0.1) in the extraction portion of the process. It is often the case that the process will have a section for scrubbing unwanted metals from the organic phase, and finally a stripping section to obtain the metal back from the organic phase.
Mixer–settlers
A mixer-settler consists of a mixing stage that often forms a suspension of two immiscible liquids followed by a settling stage that allows the liquids to separate into two layers by gravity. Mixer-settlers are typically used when a process requires longer residence times and when the solutions are easily separated by gravity. In a multistage countercurrent process, multiple mixer-settlers are installed in series with the settled output of one stage being fed to subsequent stages for further separation.Colven, 1956; Davidson, 1957Liquid–Liquid Extraction Equipment, Jack D. Law and Terry A. Todd, Idaho National Laboratory.
Centrifugal extractors Centrifugal extractors mix and separate in one unit. Two liquids will be intensively mixed between the spinning rotor and the stationary housing at speeds up to 6000 RPM. This develops great surfaces for an ideal mass transfer from the aqueous phase into the organic phase. At 200–2000 g, both phases will be separated again. Centrifugal extractors minimize the solvent in the process, optimize the product load in the solvent and extract the aqueous phase completely. Counter current and cross current extractions are easily established.
Solvation mechanism
Using solvent extraction it is possible to extract uranium, plutonium, thorium and many rare earth elements from acid solutions in a selective way by using the right choice of organic extracting solvent and diluent. One solvent used for this purpose is the organophosphate tributyl phosphate (TBP). The PUREX process that is commonly used in nuclear reprocessing uses a mixture of tri-n-butyl phosphate and an inert hydrocarbon (kerosene), the uranium(VI) are extracted from strong nitric acid and are back-extracted (stripped) using weak nitric acid. An organic soluble uranium complex [UO2(TBP)2(NO3)2] is formed, then the organic layer bearing the uranium is brought into contact with a dilute nitric acid solution; the equilibrium is shifted away from the organic soluble uranium complex and towards the free TBP and uranyl nitrate in dilute nitric acid. The plutonium(IV) forms a similar complex to the uranium(VI), but it is possible to strip the plutonium in more than one way; a reducing agent that converts the plutonium to the trivalent oxidation state can be added. This oxidation state does not form a stable complex with TBP and nitrate unless the nitrate concentration is very high (circa 10 mol/L nitrate is required in the aqueous phase). Another method is to simply use dilute nitric acid as a stripping agent for the plutonium. This PUREX chemistry is a classic example of a solvation extraction. In this case, DU = k [TBP]2[NO3−]2.
Ion exchange mechanism Another extraction mechanism is known as the ion exchange mechanism. Here, when an ion is transferred from the aqueous phase to the organic phase, another ion is transferred in the other direction to maintain the charge balance. This additional ion is often a hydrogen ion; for ion exchange mechanisms, the distribution ratio is often a function of pH. An example of an ion exchange extraction would be the extraction of americium by a combination of terpyridine and a carboxylic acid in tert-butyl benzene. In this case
DAm = k [terpyridine]1[carboxylic acid]3[H+]−3
Another example is the extraction of zinc, cadmium, or lead by a dialkyl phosphinic acid (R2PO2H) into a nonpolar diluent such as an alkane. A non-polar diluent favours the formation of uncharged non-polar metal complexes.