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Journal of Chemical Technology and Biotechnology J Chem Technol Biotechnol80:1089 1096 (2005)DOI: 10.1002/jctb.1333
Review
Use of ionic liquids as green solvents
for extractionsHua Zhao,1 Shuqian Xia2 and Peisheng Ma2
1Chemistry Program, Department of Natural Sciences and Mathematics, Savannah State University, Savannah, GA 31404, USA2School of Chemical Engineering, Tianjin University, Tianjin, China
Abstract: This review summarizes recent applications of ionic liquids (ILs) as green solvents in
extractions of a variety of substances, including metal ions, organic and bio- molecules, organosulfur from
fuels, and gases. ILs could also be used along with another green technology, supercritical fluid extraction
(SFE), for a more effective separation of products from ILs. In addition to their environmentally-benign
feature, ILs have other favorable properties over organic solvents used for extraction, such as adjustable
hydrophobicity, polarity and selectivity.
2005 Society of Chemical Industry
Keywords:ionic liquid; extraction; green technology; industrial application; supercritical fluid
INTRODUCTION
Ionic liquids (ILs) are a group of new organic
salts that exist as liquids at a low temperature
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H Zhao, S Xia, P Ma
Table 1.Examples of IL extractions of metal ions
Substances IL
Extractant/ligand/
metal chelator Reference
Alkali metals Li+, Na+, K+, Rb+, Cs+ [CnMIM][PF6] (n= 4 9) DC18C6 21,37
Na+, Cs+ [CnMIM][PF6] (n= 4, 6, 8) 18C6, DC18C6, Dtb18C6 18
Cs+ [CnMIM][Tf2N] (n= 2, 3, 4, 6, 8) BOBCalixC6 38
Na+, K+, Cs+ [CnMIM][Tf2N] (n= 2, 4, 6, 8) DC18C6, N-alkyl
aza-18-crown-6 ethers
39
Alkaline earth metals Mg2+, Ca2+, Sr2+, Ba2+ [CnMIM][PF6] (n= 4 9) DC18C6 37
Sr2+ [CnMIM][PF6] (n= 4, 6, 8) 18C6, DC18C6, Dtb18C6 18
Sr2+ [R1R2MeIM][PF6], [R1R2MeIM][Tf2N] DC18C6 19
Sr2+ [CnMIM][Tf2N] (n= 2, 4, 6, 8) DC18C6, N-alkyl
aza-18-crown-6 ethers
39
Heavy and radioactive
metals
Pb2+ [CnMIM][PF6] (n= 4 9) DC18C6 37
Cu2+, Ag+, Pb2+, Zn2+,
Cd2+, Hg2+[C4MIM][PF6] Dithizone 23
Cd2+, Co2+, Ni2+, Fe3+,
Hg2+[C4MIM][PF6], [C6MIM][PF6] PAN, TAN 20
Ag+ [CnMIM][PF6] (n= 4, 6, 8) Calyx[4]arene-bearing
pyridine
40
Cu2+, Cr6+, Zn2+ [CnMIM][BF4] (n= 1, 3, 6, 8, 10)
[CnMIM][PF6] (n= 6, 10)
None 41
Hg2+, Cd2+ TSILs None 28,35
Lanthanides (Nd3+, La3+,
Er3+, Ce3+, Sm3+, Eu3+,
Gd3+, Ho3+)
[C4MIM][PF6] CMPO 32
Actinides (Th4+, U2+, Pu4+) [C4MIM][PF6], [C4MIM][NO3], Dtb18C6, CMPO, TBP 29,34
Others Al3+ [C4MIM][Tf2N], [C6MIM][PF6]
[C8MIM][PF6]
n/a 42,43
Note: CnMIM= 1-alkyl-3-methylimidazolium; DC18C6= dicyclohexano-18-crown-6; 18C6= 18-crown-6; Dtb18C6= 4,4-(5)-di-(tert-butylcyc-
lohexano)-18-crown-6; BOBCalixC6= calix[4]arene-bis(tert-octylbenzo-crown-6); Tf2N= bis[(trifluoromethyl)sulfonyl]amide; R1R2MeIM= 1-R1-2-
R2-3-methylimidazolium (R1 = Bu, Et, or Pr; R2 = H, or Me); PAN = 1-(2-pyridylazo)-2-naphthol; TAN= 1-(2-thiazolylazo)-2-naphthol; CMPO=
octyl(phenyl)-N,N-diisobutylcarbamoylmethyl phosphine oxide; TBP= tri-n-butylphosphate.
(3) The extraction efficiency of metal complexes can
also be controlled by the pH of the system.23
Among IL extractions of metal ions, the extraction
of radioactive metals (lanthanides and actinides) has
particular industrial significance for the handling of
nuclear materials. Earlier studies in the area included
the behavior of uranium species in various ILs includ-
ing mixtures of chloroaluminate ILs and butylpyri-
dinium chloride,24,25 mixtures of chloroaluminate ILs
and [C2MIM]Cl,26
chloroaluminate ILs,27
and sev-eral RTILs.18,19,28 Recent work primarily focused on
two aspects: (1) the fundamental understanding of
ILs in nuclear chemistry such as radiochemical sta-
bility of ILs,29 superoxide ion electrochemistry in
ILs,30 and electrochemical properties of actinides in
ILs;31 (2) applications of ILs in nuclear extractions of
lanthanides32 and actinides (Table 1).29,33,34
However, the disadvantages of using extractants
are the difficulty of separating them from ILs and
the complexity of the system.28 As a new concept
introduced in the late 1990s, Task-Specific ILs
(TSILs) are designed to have targeted functionality
and, in this case, TSILs are those ILs containing metal
ion-ligating functional groups. Therefore, TSILs serve
as the hydrophobic solvent and the extractant at the
same time. TSILs containing side-chains of thiourea
derivatives and urea derivatives could dramatically
increase the partitioning of Hg2+ and Cd2+ ions from
aqueous solutions.28,35 Moreover, as indicated in a
recent review,36 TSILs are not limited to the extraction
processes; they are also versatile solvents/catalysts used
in organic catalysis, solid phase synthesis, and even
production of liquid Teflon and emulsions.
IL EXTRACTIONS OF ORGANIC/BIO/BIOFUELMOLECULES
The high solubility of charged organic molecules in
ILs has stimulated the development of organic prod-
uct recovery by these green media. As illustrated
in Table 2, phase partitions of many phenolic com-
pounds are investigated in the ILwater biphasic sys-
tems. The distribution coefficient is highly influenced
by the pH value which determines the existing form of
a phenolic compound as a conjugated acid or base.41,44
The same principle applied to the extraction of amino
acids through [BMIM][PF6] where the concentration
of the crown ether (DC18C6) also played an impor-
tant role on the amino acid recovery (Table 2).45
Meanwhile, IL biphasic systems were also used to
separate many other biologically important molecules
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Use of ionic liquids as green solvents for extractions
Table 2.Examples of IL extractions of organic/bio/biofuel molecules
Substances IL Extractant Reference
Phenolic compounds phthalic acid, aniline, 4-hydroxybenzoic
acid, benzoic acid, p-toluic acid,
benzene, chlorobenzene,
1,2,4-trichlorobenzene,
1,4-dichlorobenzene,
4,4-dichlorobiphenyl
[BMIM][PF6] None 44
Phenol, tyrosol,p-hydroxybenzoic acid [CnMIM][BF4] (n= 1, 3, 6, 8, 10)
[CnMIM][PF6] (n= 6, 10)
None 41
Chlorophenols [C4MIM][PF6], [EMIM][Beti] None 58
Amino acids Tryptophan, glycine, alanine, leucine,
lysine, arginine
[BMIM][PF6] DC18C6 45
Carbohydrates Xylose, fructose, glucose, sucrose [CnMIM][X] (n= 4, 6, 8, 10;
X= Cl, PF6, BF4
)
None 46
Glucose, sucrose, lactose, cyclodextrin [BMIM][dca] (carbohydrate solubility
is approximately 200 g l1)
None 47
Cellulose [CnMIM]X (n= 4, 6, 8) None 59
Organic acids Lactic acid, acetic acid, glycolic acid,
propionic acid, pyruvic acid, butyric
acid
[CnMIM][PF6] (n= 4, 6, 8) TBP (in some
cases)
48
Biofuels Butyl alcohol (from fermentation broth) [BMIM][PF6], [C8MIM][PF6] Pervaporation
was used
49
Antibiotic Erythromycin-A [BMIM][PF6] None 50
Hydrocarbons Olefins (such as ethylene, propylene,
and butanes) from paraffins
[CnMIM][X], [HPy][X] (n= 4, 6;
X= BF4, PF6
)
None 54,55
C4 8 diolefin (such as butadiene) from
C118 paraffins
[BMIM][BF4] None 56
Note: BMIM (or C4MIM) =1-butyl-3-methylimidazolium; EMIM= 1-ethyl-3-methylimidazolium; Beti= bis(perfluoroethylsulfonyl)imide; HPy= N-
hexylpyridinium; dca= dicyanamide.
such as carbohydrates,46,47 organic acids including
lactic acid,48 butyl alcohol (from the fermentation
broth to produce biofuels),49 and polyketide antibiotic
erythromycin-A.50 It is important to notice that car-
bohydrates are renewable and inexpensive resources
for the chemical industry. The underivatized carbohy-
drates are soluble in water but not in almost any other
solvents, which presents quite a challenge to transform
the carbohydrates. Their high solubility in ILs enables
the possibilities of transformations.47,51,52
Interestingly, an aqueous biphasic system (ABS)
was formed by contacting the hydrophilic [BMIM]Cl
with concentrated solutions of K3PO4 (or other
kosmotropic salts such as KOH, K2CO3, Na2HPO4,
and Na2S2O3).53 This finding of being able to controlthe aqueous miscibility of hydrophilic ILs is very
valuable to the separation technology, because it
enables the recycling of hydrophilic ILs, the metathesis
formation of new ILs, and even reactive separations.
These ABSs have sufficient chemical potentials to
allow the separation of organic molecules into two
phases. The partition of several short chain alcohols
(eg methanol, propanol, butanol and pentanol) in
these ABSs was found to be a strong function of the
tie line lengths.53
Hydrocarbon separation through IL extractions was
also proved possible. One method for separating
olefins (such as ethylene, propylene, and butanes)
from paraffins involved several steps:54,55 (1) salts
(such as silver) were used to form complex olefins;
(2) the olefin-containing mixture was extracted by
the ionic liquid/salt solution, and the olefins were
adsorbed; (3) the olefins were separated by desorption
after the paraffins were removed. Another process
was developed to separate C4 8 diolefin hydrocarbons
(such as butadiene) from at least one diolefin and
at least one C118 paraffin using ILs (such as
[BMIM][BF4]).56 A continuous extraction process
using IL to separate C6 9-aromatic hydrocarbons, and
higher hydrocarbons, from benzene-rich petroleum
streams has also been developed.57 These results
presented alternative green methods for separation of
hydrocarbon molecules, which is extremely valuable
to the petroleum industry and polymer-processing
industry.
IL DESULFURIZATION OF FUELS
To reduce the impact of SOx emission from fuel
burning on human health and the environment,
tighter regulations are being imposed by EPA on
oil refineries to reduce the statutory sulfur contents
of fuels.60 Conventional desulfurization of diesel
was achieved through hydroprocessing catalysts.
However, further or deep hydrodesulfurization (HDS)
requires high consumption of energy and hydrogen.
Meanwhile, the HDS process is normally only effective
for removing organosulfur compounds of aliphatic
and alicyclic types. The aromatic sulfur molecules
including thiophenes, dibenzothiophenes (DBT), and
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H Zhao, S Xia, P Ma
their alkylated derivatives are very difficult to convert
to H2S through HDS catalysts.61,62 Alternative
methods (including reactive adsorption63) of deep
desulfurization are highly demanded. One alternative
called extractive desulfurization (EDS) seems very
attractive for this purpose because of its low energy
cost, the elimination of hydrogen usage, the retaining
of the chemical structures of fuels and no requirementsof special equipment.
However, EDS through ILs seems particularly
favorable over organic solvents64 because of the use of
environmentally-benign solvents. Current research for
this purpose includes:
(1) EDS of organosulfur compounds: Bosmann
et al investigated various imidazolium- and
chloroaluminate-based ILs and found multistage
extraction was very effective in removing
sulfur;65 several ILs (eg [EMIM][BF4],
[BMIM][PF6], [BMIM][PF6]) exhibited high
selectivity in extracting aromatic sulfur and
nitrogen compounds;66 an ultra-low level of sulfur
(
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Use of ionic liquids as green solvents for extractions
(b) many organic compounds are soluble in scCO2,
enabling easy separation of products from ILs; (c) this
process can be designed as batchwise or continuous
operations. Examples of metal-catalyzed organic reac-
tions include batchwise asymmetric hydrogenation of
tiglic acid,86 batchwise hydrogenation of alkenes and
carbon dioxide,87 continuous flow hydroformylation
of oct-1-ene catalyzed by rhodium complexes,88,89
continuous flow hydrovinylation of styrene by immo-
bilized organometallic (Ni-based) catalysts.90
A number of biocatalysis reactions were achieved
successfully in ILs (see reviews, Refs6,1114), or
in scCO2 (see reviews, Refs9193). The compari-
son study of imidazolium-based ILs, scCO2 and
n-hexane for the biocatalysis of a transesterification
reaction by immobilized enzymes has shown that
the enzyme activity is strongly influenced by the
water activity.94 Recently, the combination of IL and
scCO2 to form biphasic systems has attracted a lot
of attention for biocatalysis. For example, continu-
ous processes of Candida antarctica lipase B-catalyzed
butyl butyrate synthesis and the kinetic resolution
of 1-phenylethanol processes by transesterification;95
batchwise and continuous flow processes of acyla-
tion of octan-1-ol by vinyl acetate and the reso-
lution of 1-phenylethanol both catalyzed by lipase
fromCandida antarctica;96 the transesterification reac-
tion of N-acetyl-L-phenylalanine ethyl ester with 1-
propanol catalyzed by immobilized -chymotrypsin
was conducted in scCO2 containing [C4MIM][PF6]
or [C8MIM][PF6]).97 This research concluded that
these ILs provided a rather polar environment, but
it was adjustable by nonpolar scCO2 to improve theenzyme activity.
GAS SEPARATIONS BY ILS
ILs can selectively dissolve gases. This makes them
potential solvents for gas separations.98 CO2 has rel-
atively high solubility in imidazolium-based ILs (eg
[BMIM][PF6]) as illustrated by recent experiments
and molecular modeling.99,100 A TSIL consisting of
an imidazolium ion to which a primary amine moi-
ety is covalently bonded was specifically designed
for CO2 capture.101
Ethylene and ethane havemedium solubility in [BMIM][PF6], while methane,
argon, oxygen, hydrogen, nitrogen, carbon monox-
ide have low solubility.99,102 Molecular dynamics
calculations were also consistent with experimen-
tal results that, for a given anion, the solubility
of CO2 in different ILs showed no large differ-
ence between the two cations. Another theoretical
study of gas solubility in [BMIM][PF6] was con-
ducted through the Monte Carlo simulations.103 In
this study, a molecular mechanics force field was
established to predict the thermophysical proper-
ties such as molar volumes as a function of tem-
perature. The Henrys constants for water, car-
bon dioxide and argon were also reported in this
study.
Because ILs are nonvolatile, they do not contami-
nate the gas stream during gas separation. The non-
volatility and selectivity of ILs allow them to be used in
conventional absorbers, scrubbers or supported liquid
membranes.104
SUMMARYThe first commercial process was established by BASF
AG (Ludwigshafen, Germany) to scavenge acids using
ILs.105 Several other processes developed by the same
company are in the pilot phase.104 More commercial
process developments involving ILs were presented
in a recent review.104 In summary, ILs are unique
and promising solvents for extractions because of their
non-volatility, adjustable hydrophobicity and polarity,
dissolution ability, and selectivity of gases. There is
a fundamental answer to these favorable properties:
ionic liquids are organic molecules and ionic salts at
the same time. And, they are liquids.
ACKNOWLEDGEMENTS
This project was partially supported by SSU/NIH-
EARDA grant No. 5 G11 HD 32861-07 and by an
NIH-MBRS grant.
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