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Organic-phase biological buffers for biochemical and biological research in organic media Mohamed Taha, João A.P. Coutinho CICECO-Aveiro Institute of Materials, Department of Chemistry, University of Aveiro, 3810-193 Aveiro, Portugal abstract article info Article history: Received 9 December 2015 Received in revised form 26 April 2016 Accepted 18 May 2016 Available online 01 June 2016 A long-standing problem in enzymatic catalysis in organic media is nding a buffer that keeps a constant pH, as there are no commercially available biological buffers for such media. The biological buffers such as Good's buffers that are commonly used in aqueous media are insoluble in almost all organic solvents, and there is now- adays a pressing need for a buffer for organic media. Good's buffers were designed based on sets of criteria which make them extensively used in biochemical and biological research. In this context, we show that when Good's buffers turned into ionic liquids, so-called Good's buffer ionic liquids (GB-ILs), they became highly soluble in polar organic media, such as methanol and ethanol. This implies that a huge number of organo-soluble buffers are expected to be commercially available for such solvents. Twenty ve GB-ILs (tetramethylammonium, tetraethylammonium, tetrabutylammonium, 1-ethyl-3-methy limidazolium, and choline salts of Tricine, TES, MES, HEPES, and CHES) were tested as organic-phase buffers for pure methanol, and their buffer capacities in methanol were found to be very close to that in water. A series of mixed GB-ILs was also formulated as universal buffers in methanol. Conductor-like screening model for real solvents (COSMO-RS) calculations were performed to show why GB-ILs gained high solubility in methanol. © 2016 Elsevier B.V. All rights reserved. Keywords: Good buffers ionic liquids Organic-phase buffers Biocatalysis Buffer capacity 1. Introduction Non-aqueous enzymology is becoming increasingly important for applications in biotechnological processes. It is of importance when the reactants are poorly soluble in aqueous media, which certainly speeds up reaction rates [1]. It has the ability to catalyze reactions that are kinetically or thermodynamically unfavorable in water, e.g. transesterication, thioesterication, and aminolysis [1]. Transesterication is a chemical process of exchanging acyl groups be- tween an ester and a monohydric alcohol, to produce biodiesel (monoalkyl esters) and glycerine [2]. Biodiesel produced by the transesterication of oils or animal fats is a promising alternative diesel fuel regarding the limited resources of fossil fuel and the environmental impacts [2]. There are many monohydric alcohols used for biodiesel production, such as methanol, ethanol, propanol, 2-opropanol, and bu- tanol. Enzyme-catalyzed transesterication, especially those using li- pase, for the production of biodiesel allow using alcohol in a solvent free system [2]. Most enzymes are, however, less active in organic solvents or in low- water concentration media and they must be stabilized and protected from inactivation. An essential issue in this context is that of enzyme ionization, which is a key determinant of its activity. The enzyme can have its activity changed signicantly by adding or removing protons. The catalytic activity of enzymes in both aqueous and organic media is strongly affected by the pH displaying an optimum pH. The pH effect upon the enzymatic activity can be gauged from examples such as the subtilisin (cross-linked crystals) that can be activated more than 100- fold in pentanone by adding a buffer[3], or the report that the activity of enzymes in organic solvents is highly dependent on the pH of the last aqueous solution on which the enzyme was lyophilized (pH memory phenomenon) [3], the protonation state of the enzyme's ionisable groups being retained in the organic solvent. The ionization state of an enzyme in organic solvents can thus be manipulated by lyophilization of the enzyme from an aqueous buffered solution. This is an unpractical and expensive approach that can be thwarted since the pH memory can be altered if acidic or alkaline species are used in the reaction mixture [46]. The use of buffers soluble in organic phases to control the pH of a non-aqueous medium would be a more adequate approach. Unfortu- nately, most known buffers are insoluble in organic solvents due to their charged nature and high polarity, being the development of alternative buffers for such organic media a pressing need. Buffers for organic phases can be formulated from hydrophobic bases or acids and their salts, such as combinations of triisooctylamine with its hydrochloride, or of triphenylacetic acid with its sodium salt [7,8]. Dolman et al. synthesized more hydrophobic buffers based on functionalized, dendritic polybenzylethers [9]. These organo-soluble buffers, although limited in number, effectively erase the enzyme's pH Journal of Molecular Liquids 221 (2016) 197205 E-mail address: [email protected] (J.A.P. Coutinho). http://dx.doi.org/10.1016/j.molliq.2016.05.052 0167-7322/© 2016 Elsevier B.V. All rights reserved. Contents lists available at ScienceDirect Journal of Molecular Liquids journal homepage: www.elsevier.com/locate/molliq

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Page 1: Journal of Molecular Liquids - Pathpath.web.ua.pt/publications/j.molliq.2016.05.052.pdf · 1. Introduction Non-aqueous enzymology is becoming increasingly important for applications

Journal of Molecular Liquids 221 (2016) 197–205

Contents lists available at ScienceDirect

Journal of Molecular Liquids

j ourna l homepage: www.e lsev ie r .com/ locate /mol l iq

Organic-phase biological buffers for biochemical and biological researchin organic media

Mohamed Taha, João A.P. CoutinhoCICECO-Aveiro Institute of Materials, Department of Chemistry, University of Aveiro, 3810-193 Aveiro, Portugal

E-mail address: [email protected] (J.A.P. Coutinho).

http://dx.doi.org/10.1016/j.molliq.2016.05.0520167-7322/© 2016 Elsevier B.V. All rights reserved.

a b s t r a c t

a r t i c l e i n f o

Article history:Received 9 December 2015Received in revised form 26 April 2016Accepted 18 May 2016Available online 01 June 2016

A long-standing problem in enzymatic catalysis in organic media is finding a buffer that keeps a constant pH, asthere are no commercially available biological buffers for such media. The biological buffers such as Good'sbuffers that are commonly used in aqueous media are insoluble in almost all organic solvents, and there is now-adays a pressing need for a buffer for organicmedia. Good's buffers were designed based on sets of criteria whichmake them extensively used in biochemical and biological research. In this context, we show that when Good'sbuffers turned into ionic liquids, so-called Good's buffer ionic liquids (GB-ILs), they became highly soluble inpolar organic media, such as methanol and ethanol. This implies that a huge number of organo-soluble buffersare expected to be commercially available for such solvents. Twenty five GB-ILs (tetramethylammonium,tetraethylammonium, tetrabutylammonium, 1-ethyl-3-methy limidazolium, and choline salts of Tricine, TES,MES, HEPES, and CHES) were tested as organic-phase buffers for pure methanol, and their buffer capacities inmethanol were found to be very close to that in water. A series of mixed GB-ILs was also formulated as universalbuffers in methanol. Conductor-like screening model for real solvents (COSMO-RS) calculations were performedto show why GB-ILs gained high solubility in methanol.

© 2016 Elsevier B.V. All rights reserved.

Keywords:Good buffers ionic liquidsOrganic-phase buffersBiocatalysisBuffer capacity

1. Introduction

Non-aqueous enzymology is becoming increasingly important forapplications in biotechnological processes. It is of importancewhen the reactants are poorly soluble in aqueous media, whichcertainly speeds up reaction rates [1]. It has the ability to catalyzereactions that are kinetically or thermodynamically unfavorable inwater, e.g. transesterification, thioesterification, and aminolysis [1].Transesterification is a chemical process of exchanging acyl groups be-tween an ester and a monohydric alcohol, to produce biodiesel(monoalkyl esters) and glycerine [2]. Biodiesel produced by thetransesterification of oils or animal fats is a promising alternative dieselfuel regarding the limited resources of fossil fuel and the environmentalimpacts [2]. There are many monohydric alcohols used for biodieselproduction, such as methanol, ethanol, propanol, 2-opropanol, and bu-tanol. Enzyme-catalyzed transesterification, especially those using li-pase, for the production of biodiesel allow using alcohol in a solventfree system [2].

Most enzymes are, however, less active in organic solvents or in low-water concentration media and they must be stabilized and protectedfrom inactivation. An essential issue in this context is that of enzymeionization, which is a key determinant of its activity. The enzyme can

have its activity changed significantly by adding or removing protons.The catalytic activity of enzymes in both aqueous and organic media isstrongly affected by the pH displaying an optimum pH. The pH effectupon the enzymatic activity can be gauged from examples such as thesubtilisin (cross-linked crystals) that can be activated more than 100-fold in pentanone by adding a “buffer” [3], or the report that the activityof enzymes in organic solvents is highly dependent on the pH of the lastaqueous solution on which the enzyme was lyophilized (pH memoryphenomenon) [3], the protonation state of the enzyme's ionisablegroups being retained in the organic solvent. The ionization state of anenzyme in organic solvents can thus be manipulated by lyophilizationof the enzyme from an aqueous buffered solution. This is an unpracticaland expensive approach that can be thwarted since the pHmemory canbe altered if acidic or alkaline species are used in the reaction mixture[4–6]. The use of buffers soluble in organic phases to control the pH ofa non-aqueous medium would be a more adequate approach. Unfortu-nately,most known buffers are insoluble in organic solvents due to theircharged nature and high polarity, being the development of alternativebuffers for such organic media a pressing need.

Buffers for organic phases can be formulated from hydrophobicbases or acids and their salts, such as combinations of triisooctylaminewith its hydrochloride, or of triphenylacetic acid with its sodium salt[7,8]. Dolman et al. synthesized more hydrophobic buffers based onfunctionalized, dendritic polybenzylethers [9]. These organo-solublebuffers, although limited in number, effectively erase the enzyme's pH

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198 M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

memory and control its protonation state [10]. Solid-state acid–basebuffers have been also proposed for use in organic media [10–14].These solid buffers consist of a zwitterionic compound (Good's buffersamong the others) and its sodium salt. Although these buffers wereable to control the ionization state of the catalytic triad of subtilisin inorganic solvents [13], they failed with papain [10].

Recently, ionic liquids with buffering characteristics has been syn-thesized [15–17]. Room temperature ionic liquids (RTILs) are normallydescribed as molten salts which are liquid at room temperature, orsalts melting below 100 °C. The ILs have enhanced the enzyme activityand stability in comparison to other solvent media [18,19]. Very limitedattention, however, has been devoted to prepare ILs that can control thepH of non-aqueous systems. Yuan and co-workers [15–17] have synthe-sized buffer-like ILs by neutralization of imidazolium hydroxides withpolybasic acids such as the phthalic, tartaric, and phosphoric acid.These ILs are miscible with polar solvents such as methanol, dichloro-methane, and dimethylformamide (DMF). MacFarlane et al. [20] havedescribed that hydrated ILs, such as choline dihydrogenphosphatehave buffering action. Although these buffer-like ILs have good solubil-ity in the above-mentioned organic solvents, but their anions are notinert for one reason or another. For example, using phosphate ions pre-cipitates metal ions such as, calcium, zinc, or magnesium, metals thatare essential to maintain the biological function of some enzymes [21,22].

Most biological buffers used today were developed by Good and hiscolleagues [21,22] and are known as Good's buffers (GBs). Their acro-nyms are spread in literature and laboratorymanuals, and have becomenewwords; i.e., HEPES buffer appears as the word Hepes. These buffersare zwitterionic amino acids, eitherN-substituted taurine or glycine de-rivatives, which provide good coverage of the physiological pH range(6.1–10.4). Good set forth several criteria to define the best buffers forbiochemical systems, his buffers fulfilling most of these criteria: Thebuffers should be chemically inert; non-toxic; present no absorptionin the UV–visible region; no formation of complexes with metal ions;be easy to prepare and inexpensive; and their pKa values should notvary with temperature. They should also ideally have high water solu-bility and low lipid solubility so that they do not permeate the cellmem-branes. Good's buffers are however highly soluble inwater but insolublein pure organic solvents such as aliphatic alcohols, cyclic ethers, acetone,and acetonitrile [23,24]. They cannot thus be used for controlling the pHin organic solvents. The high affinity of GBs to water molecules is due totheir high polarity [23,24].

We have recently introduced a new class of buffer-like ILs, Good'sbuffer ionic liquids (GB-ILs), which derived from Good's buffers(e.g., TES, TAPS, TAPSO, HEPES, EPPS, MES, MOPS, MOPSO, CHES, CAPS,CAPSO, BES, Bicine, and Tricine) as anions and several cations such astetramethylammonium ([N1111]+), tetraethylammonium ([N2222]+),tetrabutylammonium ([N4444]+), 1-ethyl-3-methy limidazolium([C2mim]+), and cholinium ([Ch]+) [25–29]. These GB-ILs have provento be remarkably effective as biological buffers and protein stabilizers inaqueous solution [25–30]. Some of these GB-ILswere also found to formaqueous biphasic systems (ABS) whenmixedwith aqueous solutions ofinorganic salts, organic salts, or PPG 400 (poly(propylene)glycol with amolecularweight of 400 gmol−1), andwere successfully used to extractbiomolecules such as protein and antibody [25–30] without adding ex-ternal buffers. Here, we have observed for the first time that GB-ILs, un-like common GB, are highly soluble in polar organic solvents, e.g.methanol and ethanol. The goal of this work is to investigate whetherGB-ILs could still act as buffering agents in these organic solvents. Thepresence of the buffering action of GB-ILs is confirmed by measuringtheir pH-profiles in methanol as an example. The reason of choosingmethanol is the most widely used alcohol for biodiesel productionusing enzymatic transesterification process. The reasons behind thehigh solubility of GB-ILs in methanol, as compared to the conventionalGood buffers, are explained theoretically by conductor-like screeningmodel for real solvents (COSMO-RS) calculations.

2. Materials and methods

2.1. Materials

The buffers, MES (purity N99 wt%), TES (purity N99 wt%), HEPES(purity N99.5 wt%), Tricine (purity N99 wt%), and CHES (purityN99wt%),were obtained from Sigma–Aldrich Chemical Co. The hydrox-ides, tetramethylammonium (25 wt% in H2O), tetraethylammonium(25 wt% in H2O), tetrabutylammonium (40 wt% in H2O), and 1-ethyl-3-methylimidazolium (10 wt% in H2O), were also provided by Sigma–Aldrich Chemical Co. (USA). Sodium hydroxide pellets obtained fromEka Chemicals, and 0.05 M HCl-methanol solution was prepared from0.5 M HCl-methanol solution obtained from Sigma–Aldrich ChemicalCo. (USA). Methanol (HPLC grade, purity N99.9%) was purchased fromFisher Scientific and acetonitrile (purity N99.7) was supplied fromLab-Scan. Purified water was obtained by aMilli-Q plus 185 water puri-fying system.

2.2. Synthesis and characterization of Good's buffer ionic liquids

The GB-ILs, [C2mim][GB], [N1111][GB], [N2222][GB], [N4444][GB], and[Ch][GB], were synthesized by neutralizing a slight excess of equimolarGB with the aqueous corresponding organic hydroxide aqueous solu-tion as described in our earlier papers [24,25], where GB=MES, Tricine,TES, HEPES, and CHES. Brefiely, an aqueous solution of the organic hy-droxidewas added dropwise to a slightly excess equimolar buffer aque-ous solution. The solution was stirred magnetically at ambientconditions for about 12 h. The reaction mixture was evaporated at60 °C under vacuumusing a rotary evaporator to obtain a viscous liquid.Then, amixture of acetonitrile andmethanol (1:1)was added to the vis-cous liquid and stirred vigorously at room temperature for 1 h to precip-itate the unreacted buffer. The solution was then filtered to remove anyprecipitate presented. The synthesized GB-ILs were purified bywashingwith acetone several times. The solvent mixture was evaporated andGB-IL product was then dried under vacuum for 3 days at room temper-ature. Thewater content of GB-ILswasmeasured by Karl–Fischer coulo-meter (Metrohm Ltd., model 831) and it was found to be less than0.05wt%. The chemical structures of the GB-ILs were confirmed, respec-tively, by 1H and 13C NMR spectroscopy (Bruker AMX 300) operating at300.13 and 75.47 MHz, and presented in our earlier papers [25,26]. Thechemical structures of GB-IL are shown in Fig. 1.

2.3. Potentiometric titrations

pH titration profiles were performed in double-walled glass vesselusing an automatic titrator (Metrohm 672) equipped with a dosimat655 and a solvotrode (Metrohm 6.0229.100) for pH measurements innon-aqueous acid-base. The pH electrode was calibrated in aqueoussolution with two standard buffers of pH 4.0 and 7.0. The temperatureof the titration vessel was controlled at 298.2 ± 0.1 K by thermostaticwater bath with continuous magnetic stirring. For measuring thepH profiles of GBs in water, 10 mL of 0.05 M GB was freshly preparedin water and titrated with 0.05 M NaOH. The pH profiles of GB-ILsin pure methanol were carried out by titrating 10 mL of 0.05 M GB-ILsprepared in methanol with 0.05 M NaOH/HCl dissolved in methanol.At least two repeated measurements were performed for each pHprofile.

Since the pH meter is calibrated using in aqueous solution, thepHmethanol reading obtained in non-aqueous medium differs by anamount, δ, from the pHwater reading obtained when the pH meter stan-dardized using aqueous buffer solution. The δ value for puremethanol iswell known (−2.24 in themolarity scale), and, therefore, experimentalpHwater allow to get the pHmethanol, by means of pHmethanol =pHwater + 2.24 [31–35].

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Fig. 1. Chemical structures of the studiednGB-ILs.

199M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

2.4. COSMO-RS calculations

The σ-profiles of HEPES zwitterion, [HEPES] anion, [N1111] cation,water, and methanol were performed by optimizing their geometriesat RI-DFT/BP/TZVP level and applying COSMO continuum solvationmodel, as implemented in TURBOMOLE 6.1 quantum chemical programpackage [36]. The COSMOtherm (version C30_1401) software, based onCOSMO-RS model, was used to predict the excess free energies, excessenthalpies, and solubility of GB/GB-ILS in alcohol [37,38]. The solubilityis calculated from Eq. (1),

log10 xj� � ¼ log10 exp μpure

j −μsolventj −Δ Gj;fusion

� �=RTÞ

h ið1Þ

COSMOtherm can directly calculate the chemical potentials μjpure ofall pure compounds j and the chemical potentials μjsolvent at infinite dilu-tion. The xj refers to the solubility in mole fraction, and R is the ideal gasconstant and T is the absolute temperature. A quantitative structureproperty relationship (QSPR) were used to calculate the free energy offusion, Δ Gj , fusion , of GB/GB-ILS. The COSMO files of the two ions ofGB-ILs were merged into a meta file.

The contact probability of GB/GB-ILs and methanol was computedby COSMOtherm program which is based on COSMO-RS theory. Thenet contact probability (PAB) between two molecules, A and B, is givenby Eq. (2),

PAB ¼ xB ∑i∈A∑i∈B Ai Aj γi γ j e−Eij

�kT

AAtotal Atotal

ð2Þ

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l

Fig. 2. (a) The pH profiles of the choline-based GB-ILs in pure methanol at 20 °C; (■)[Ch][MES], ( ) [Ch][HEPES], ( ) [Ch][CHES], and ( )[Ch][TES]. (b) The pH profile of (Δ)[Ch][Tricine] in pure methanol at 293.2 ± 0.1 K. Negative values correspond to titrationwith acid, positive values titration with alkali.

Table 1The mid-point pH and buffer capacity of the N-substituted taurine GB-ILS in methanol at293.2 K.

GBILs Mid-pointpHa

Buffercapacityb

GB/GBILs Mid-pointpH

Buffercapacityb

MESc 6.0 0.016 TESc 7.4 0.022[Ch][MES] 7.1 0.022 [Ch][TES] 9.7 0.028[N4444][MES] 7.9 0.021 [C2mim][TES] 10.5 0.020[N1111][MES] 8.0 0.019 [N4444][TES] 10.5 0.023[N2222][MES] 8.0 0.022 [N2222][TES] 10.8 0.020[C2mim][MES] 8.0 0.021 [N1111][TES] 11.0 0.020HEPESc 7.5 0.024 CHESc 9.3 0.019[Ch][HEPES] 8.4 0.023 [Ch][CHES] 9.9 0.022[N4444][HEPES] 9.1 0.021 [N4444][CHES] 10.6 0.024[C2mim][HEPES] 9.2 0.021 [N2222][CHES] 10.8 0.023[N2222][HEPES] 9.3 0.022 [C2mim][CHES] 10.8 0.024[N1111][HEPES] 9.3 0.019 [N1111][CHES] 11.1 0.022

a Not: The buffer offers significant buffering capacity when the solution pH is within ~1unit of the mid-point pH (pKa2).

b Buffer capacity is a measure of a buffer's ability to resist change in pH upon the ad-dition of acid or base; andmathematically, buffer capacity (β) is defined asβ ¼ dCb

�dðpHÞ ¼

−dCa�dðpHÞ , where Cb and Cb, are the number of moles of strong base or acid added per

liter.c The mid-point pH and buffer capacity of the GB in water.

200 M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

where xB is themole fraction of molecule B; i and j refer to indices of thesurface segments of molecule A and B, respectively; Ai, Aj represent thesegment surface area for surface segments of molecule A and B, respec-tively; γi, γj are the segment activity coefficients for surface segments ofmolecule A and B, respectively; Eij is the interaction energy betweensegments i and j; k is the Boltzmann constant; T is the temperature; Atota-Ais the total surface area ofmolecule A; and Atotal is the total surface areaof all molecules in the mixture.

3. Results and discussion

The solubility assays have shown that all the investigated GB-IL, un-like common GB, are soluble in organic solvents. These compoundswere found to be highly soluble in highly polar organic solvents, suchas methanol and ethanol. The solubilities of GB-ILs were poor in lesspolar organic solvents, such as 1-propanol, 2-propanol, 1-butanol, 1-pentanol, 1-hexanol, 1-octanol, acetonitrile, DMF, DMSO, chloroform,and dichloromethane. However, the solubility of GB-ILs in these sol-vents or others can be manipulated by choosingmore hydrophobic cat-ions that are miscible in these solvents.

To examine whether these GB-ILs can be applied as buffers in thepolar organic solvents, their pH profiles have been measured in puremethanol, as an example. Fig. 2 shows the pH profiles of the choline-based GB-ILs in pure methanol at 293.2 ± 0.1 K, as a representative.The investigated Good's buffers have two dissociation constants(pKa's), the pKa1 is due to the deprotonation of the carboxylic or sulfon-ic group, and the pKa2 is due to deprotonation of the protonated aminogroup. The inflection point appeared at high pH values of those titrationcurves which is attributed to the pKa2 of the GB-ILs. The buffer region isthe region of moderate slope before the inflection point. At the middleof this region, the concentrations of the deprotonated and protonatedspecies are equal, and according to the Henderson-Hasselbalch equa-tion, the buffering capacity is best at this point because the pH will beequal to pKa2. We can clearly see from these figures that all the GB-ILsinmethanol have buffering regions. Themid-point pH and buffer capac-ity of the GB-ILs in puremethanol are reported in Tables 1 and 2, togeth-er with the corresponding GBs in pure water for comparison purpose.Interestingly, all the obtained GB-ILs show high buffer capacities inmethanol. The buffer capacity of the N-substituted taurine-based GB-ILs in methanol are very close that of their respective GBs in water,whereas the buffer capacity of Tricine-based GB-ILs (~0.02) are almosthalf of that of Tricine in pure water (0.04). It is known that buffer capac-ities ranging from 0.01–0.1 are usually adequate for biological studies.The half neutralization values are different from those of the corre-sponding Good's buffers in water. This is due to the effect of methanolon the protonation constant of the amine group. The Tricine-basedGB-ILs (Fig. 2b) in pure methanol show an unexpectedly second bufferregion relative to the protonation of the carboxylic acid (pKa1) aroundpH 6.0. The observed increases in the pKa1 (~6.0) compared to that ob-tained in pure aqueous medium (pKa1 = 2.042 at 293.2 ± 0.1 K [39])are attributed to the effect of methanol. The protonation equilibriumof [Ch][Tricine] is shown in Fig. 3.

Few universal buffers have been developed before [40], but theywere not suitable for biological research. Usually, the enzyme activ-ity is measured at different pH values using various buffers to main-tain the solution buffer capacity. Another aim of the current studywas to formulate a set of universal buffers with general suitabilityfor enzyme activity assay that span a large pH range in pure metha-nol. The buffers MES, HEPES, and CHES have negligible metal-binding affinity which is making them suitable alternatives for for-mulating biocompatible universal buffers. The high affinity of Tricinefor divalent and trivalent metal ions [41,42] makes it incompatiblewith solutions containing metal ions. Fig. 4 shows universal GB-IL([Ch][MES] + [Ch][HEPES] + [Ch][CHES]) in pure methanol at293.2 ± 0.1 K. The pH profile was nearly linear from pH 6.2 to 10.6.We also formulated another universal buffers in methanol by using

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Table 2The mid-point pH and buffer capacity of Tricine-ILs in methanol at 293.2 K.

GB-ILs Mid-point pH Buffer capacity

1st 2nd 1st 2nd

Tricinea – 8.3 – 0.040[N1111][Tricine] 5.9 11.3 0.016 0.019[N2222][Tricine] 5.9 11.2 0.015 0.018[N4444][Tricine] 6.0 11.0 0.009 0.017[Emim][Tricine] 6.0 11.2 0.010 0.018

a The mid-point pH and buffer capacity of Tricine in water.

Fig. 4. (a) The pH profiles of the choline-based universal GB-ILs;(a) [Ch][MES] + [Ch][HEPES] + [Ch][CHES] and (b)[Ch][MES] + [Ch][Tricine] + [C][CHES] in pure methanol at 293.2 ± 0.1 K. Negativevalues correspond to titration with acid, positive values titration with alkali.

201M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

Tricine-based buffers as substitute for HEPES buffers([Ch][MES] + [Ch][Tricine] + [Ch][CHES]) but it can be used onlyin free metal-ion systems. It covers more working pH range 4.0 to11.2.

It was expected that titration of GB-ILs with acid in pure methanolcould form precipitates due to the formation of HEPES zwitterion,which is insoluble in methanol. No any precipitate was seen duringthe titration of the studied GB-ILs, suggesting that the zwitterionmight form a soluble complex with the cation.

To understand the reasons behind the high solubility of GB-ILs in thepolar organic solvent, we used the COSMO-RSmethod to provide theσ-profile of the individual compounds of [N1111][HEPES] in methanol andwater, as an example. The σ-profile depicts the surface charge densitydistribution on the molecular surface, which allows us to obtain richquantitative information about the polarity of molecules. The σ-profileis divided into three regions (Fig. 5); H-bond donor, H-bond acceptor,and non-polar region between them. The H-bond cutoff is 0.01 e Å−2.It is clear from the representative results in Fig. 5 that the zwitterionicHEPES buffer shows a strongly negative polar peak at about0.016 e Å−2 (deep red) arising from the oxygen's sulfonic and hydroxylgroups as well as the tertiary amine nearby the hydroxyl group, and onthe other side strongly positive polar peaks arising from the protonatedamine and the hydroxyl's hydrogen at −0.01, −0.017, and −0.02e·Å−2 (deep blue). While the peak at−0.005 e Å−2 is due the carbonsof the yellow-green regions. From the σ-profile of HEPES buffer, it canbe easily seen that HEPES zwitterion is a strongly polar compound hav-ing potentially hydrogen bonding groups; and itwould be expected thata dense network of intermolecular hydrogen bonds exists betweenHEPES molecules themselves in the solid structure. Two crystal struc-tures of HEPES have been solved, one crystallized from hot methanol[43] and the other fromwater [44–46]. A dense network of intermolec-ular hydrogen bonds via Osulfate⋯H—N, and N⋯H—O was found [46].The σ-profile of water has almost symmetric peaks at about±0.015 e Å−2 resulting from the two polar hydrogen atoms and thelone pairs of the oxygen atom. On the other hand, we can see from the

Fig. 3. The protonation equilibrium of [Ch][Tricine].

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Fig. 5. σ-Profiles of HEPES (black line), [HEPES] anion (blue line), [N1111] cation (cyanline), water (red line) and methanol (green line). (For interpretation of the references tocolor in this figure legend, the reader is referred to the web version of this article.)

Fig. 6. Contact probability of the HEPES + methanol and [N1111][HEPES] + methanol at298.2 K using COSMO-RS at equal molar concentrations.

202 M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

σ-profile of methanol that the acceptor peak of the oxygen has almostthe same polarity, but with less breadth, while the donor peak of thehydroxyl's hydrogen is almost half of the water's hydrogen. Further,there is a non-polar peak resulting from the CH3 group. The HEPES zwit-terion is highly soluble in water and insoluble inmethanol since the po-larity of the water molecules is able to break the dense intermolecularhydrogen bonds between HEPES molecules, while this is not the casewith solvents of low polarity, such as methanol. Removing the protonof the protonated amine group of HEPES by tetramethylammonium hy-droxide shifts the strongly positive polar peaks of HEPES toward thenon-polar region, as shown from the σ-profile of [HEPES] anion. Thisweakens the intermolecular hydrogen network among HEPES mole-cules, and enhances the solubility of HEPES in methanol and water.The peak at−0.01 e Å−2 arising from the protonated amine's hydrogendisappears and the peak of the hydroxyl's hydrogen is superposed onthe hydroxyl peak of methanol. The negative polar peak of HEPES is fur-ther shifted to more positive value, 0.017 e Å−2 [HEPES] anion. Thetetramethylammonium cation, [N1111] cation has two peaks at(−0.005 and −0.009) e Å−2, where the higher peak is the dominantas shown in Fig 5. The σ-profiles of [HEPES] anion and [N1111] cationare complementary; i.e., the negatively polar region of [HEPES] anionmatches the positively polar nitrogen and hydrogen atoms of [N1111]cation. This creates a high probability for ion pair formation between[HEPES] anion and [N1111] cation, especially in pure methanol due itslow dielectric medium, as compared to water, in which the oppositecharges interact more strongly.

The contact probability of HEPES zwitterion and methanol mole-cules, as well as [N1111][HEPES] andmethanol at equal molar concen-trations, as a representative, was obtained from COSMO-RS based onthe lowest energy contact and plotted in Fig. 6. The result clearlyshows that HEPES–HEPES interaction is dominant in HEPESzwitterion + methanol mixture, in reasonable agreement with thatexpected from σ-profile of HEPES. The geometries of complexesbased on the criterion of lowest interaction energy, obtained fromthe contact probability calculation are given in Fig. 7. On visualizing

the contact probability of HEPES-HEPES interaction in methanol, areasonable agreement between the molecule geometry for contact-complex of HEPES-HEPES (Fig. 7) and the crystal structure ofHEPES [39] were achieved. The contact probability between HEPESmolecules is reduced to almost half when HEPES buffer turned to[N1111][HEPES], [HEPES] anion–[HEPES] anion interaction. This isdue to the ion-pair formation (Fig. 7) since the contact probabilitiesof [HEPES] anion–[HEPES] anion and [HEPES] anion – [N1111] cationare nearly equal. Moreover, the contact probability of [HEPES]anion–methanol is almost equal to that of [N1111] cation –methanol,and their contact geometries are shown in Fig. 7. Thus, the ion-pairformation plays an important factor in governing the solubility of[N1111][HEPES] in methanol.

Aiming to investigate effect of increasing the alky chain length ofthe tetraalkylammonium-based GB-ILs on the solubility of these ILsin monohydric alcohols. The solubilities of HEPES zwitterion,[N1111][HEPES], [N2222][HEPES], [N4444][HEPES] in methanol, ethanol,propanol, and butanol were predicted by COSMO-RS model (Table 3).The solubility of HEPES in alcohols is negligible. The solubility ofthe HEPES-based GB-ILs in alcohol follows the order,[N1111][HEPES] b [N2222][HEPES] b [N4444][HEPES]; thus, increasing thealkyl chain length increases the solubility of GB-ILs. The solubility ofGB-IL decreases with decreasing the polarity of alcohol,methanol N ethanol N propanol N butanol.

The suitability of COSMO-RS to predict the excess properties and an-alyze the molecular interactions in the binary mixtures of ionic liquidsand solvents such as alcohols [47,48] has been studied by severalgroups. Given this background, here we predict the excess free energies(Gm

E ) and excess free enthalpies (HmE ) ofmixing of HEPES zwitterion and

tetraalkylammonium-based HEPES ILs with alcohols at 298.15 K, usingCOSMO-RS model, to provide insight into the competitive interactionsin these mixtures (Figs. 8-10). The excess free energies (Gm

E ) of HEPESzwitterion, [N1111][HEPES], [N2222][HEPES], and [N4444][HEPES] inmethanol were predicted at 298.15 K and given in Fig. 8. It is observedthat higher free energies is obtained in the order of[N4444][HEPES] N [N2222][HEPES] N [N1111][HEPES] ≫ HEPES zwitterion.Themixing of HEPES andmethanol shows positiveGm

E values, indicatingunfavorable interactions. While, negative Gm

E values are obtained formixing of tetraalkylammonium-based HEPES ILs with methanol, sug-gesting favorable energetic interactions. Similar behavior is obtained forHmE values for these systems (Fig. 9a), indicating the stronger interac-

tions between GB-ILs and methanol. The presence of these interactionsplays an important role in solubility of GB-ILs in methanol. The estima-tions of Hm

E values using the COSMO-RS model arise from summing the

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Fig. 7. Themolecule geometry for contact-complexes obtained from the contact probability calculation using COSMO-RSmethod at a dihedral angle of 0 degree. The atomdistances are inangstroms.

203M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

three molecular interactions (Eq. 3), namely, electrostatic/misfit, HMFE ;

hydrogen bonds, HHBE ; and van der Waals forces, HVdW

E .

HE ¼ HEMF þ HE

HB þ HEVdW ð3Þ

Thus, thismodel can be used to analyze the contribution of each spe-cific intermolecular interaction. The HMF

E , HHBE , HVdW

E values over thewhole composition range are also depicted in Fig. 9(b–d). The hydrogenbonding and van der Waals forces contribute largely to exothermicallyof the mixture, while the electrostatic misfit enthalpy, HMF

E contributesendothermicity. It can be clearly seen that the dominant interaction isthe hydrogen bonding due to strong H-bond acceptor and donor ofHEPES anion. Since the interaction HHB

E increases with decreasing thepolarity of the cations. Therefore, an increase in the hydrophobicity ofthe cation is accompanied by a simultaneous decrease in the[cation]–[anion] thatmay enhance the ability of anion to formhydrogenbonds with methanol and then lead to an increase in the interaction ofGB-ILs with methanol. On the other hand, the decreases in solubilityof HEPES zwitterion and [N1111][HEPES] with the decrease in polarityof alcohol (increase of the carbon length from methanol to butanol)can be explained on the basis from the excess free energies as given in

Table 3The solubility of HEPES, [N1111][HEPES], [N2222][HEPES], [N4444][HEPES], and[C2mim][HEPES] in monohydric alcohols, which predicted by COSMO-RS model.

Solutes Molar solubility (M)

Methanol Ethanol Propanol Butanol

HEPES 0.0022 0.0001 0.0000 0.0000[N1111][HEPES] 0.1950 0.0096 0.0026 0.0005[N2222][HEPES] 1.7365 0.3556 0.1875 0.0502[N4444][HEPES] 2.0003 1.5963 1.5592 0.9473

Fig. 10. The interaction free energies of water HEPES zwitterion or[N1111][HEPES] are decreased with decreasing the polarity of alcohol,and the Gm

E values of [N1111][HEPES] are much greater than those ofHEPES zwitterion.

Activity coefficients of methanol (γmethanol ) in the presence ofHEPES and tetraalkylammonium–based HEPES ILs predicted fromCOSMO-RS, at 298.15 K, are plotted in Fig. 11. The predictedγmethanol in the GB-ILs shows negative deviations to the ideality,confirming the favorable interaction with methanol, with the order[N4444][HEPES] N [N2222][HEPES] N [N1111][HEPES]. While the activity

Fig. 8. The predicted excess free energies (GmE ) of HEPES zwitterion, [N1111][HEPES],

[N2222][HEPES], and [N4444][HEPES] in methanol at 298.15 K, using the COSMO-RSmodel; xmethanol refers to the mole fraction of methanol.

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Fig. 9. The excess enthalpies, HmE (a), Hm,HB

E (b), Hm ,VdWE (c), Hm ,MF

E (d), for methanol + HEPES zwitterion, [N1111][HEPES], [N2222][HEPES], or [N4444][HEPES] systems at 298.15 K using theCOSMO-RS; xmethanol refers to the mole fraction of methanol.

204 M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

coefficients of methanol in HEPES zwitterion presents positive devi-ation to ideality, confirming the unfavorable interaction. Further-more, the predicted activity coefficients of methanol, ethanol,propanol, or butanol in the presence of HEPES ziwtterion and[N1111][HEPES] at 298.15 K are given in Fig. 12. All these systemsshow higher γmethanol than one showing unfavorable interaction be-tween alcohol and HEPES, according to the following increasingorder: butanol N propanol N ethanol N methanol. The ranking forthese alcohol in [N1111][HEPES] follows the same order of that inHEPES, but the γmethanol were less than one expecting butanol atmole fraction lower than 0.55. From the above discussion it is clearthat the interaction behavior based on the predicted γmethanol by

Fig. 10. The excess free energies, GmE , HEPES in (-■-, methanol), ( , ethanol), ( ,

propanol), and ( , butanol), as well as the excess free energies of [N1111][HEPES], (-□-, methanol), ( , ethanol), ( , propanol), and ( , butanol) at 298.15 K using theCOSMO-RS; xmethanol refers to the mole fraction of methanol.

COSMO-RS has been found to be the same interaction behavior withGmE and Hm

E results.

4. Conclusion

This is the first report addressing that the non-toxic and biocompat-ible Good's buffer ionic liquids could be used as biological buffers for or-ganic solvents, as there are no commercially available biological buffersfor suchmedia. This is vitally important as it is known that the future ofthe non-aqueous enzymology depends on reliable biological buffer sys-tems in non-aqueous media. GB-ILs were highly soluble in methanoland ethanol. The buffer capacity of 25 GB-ILs were measured in pure

Fig. 11. Activity coefficient of methanol, γmethanol, as a function of mole fraction ofmethanol for (-■-, HEPES), ( , [N1111][HEPES]), ( , [N2222][HEPES]), and( ,[N2222][HEPES]) at 298.15 K using the COSMO-RS model.

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Fig. 12. Activity coefficient of methanol, γmethanol, as a function of mole fraction ofmethanol for HEPES in (-■-, methanol), ( , ethanol), ( , propanol), and ( ,butanol), as well as activity coefficient of methanol for [N1111][HEPES], (-□-, methanol),( , ethanol), ( , propanol), and ( , butanol), at 298.15 K using the COSMO-RS.

205M. Taha, J.A.P. Coutinho / Journal of Molecular Liquids 221 (2016) 197–205

methanol. All the studied GB-ILs show high buffer capacities in metha-nol. The unexpected solubility of theses ILs in organic solvent has beenexplained using COSMO-RS calculations. Universal GB-IL buffers wereformulated to cover a wide pH range for use in enzyme activity assaysin pure methanol.

Acknowledgment

This work was financed by national funding from Fundação para aCiência e a Tecnologia (FCT, Portugal), European Union, QREN, FEDERand COMPETE for funding the CICECO (project PEst-C/CTM/LA0011/2013), QOPNA (project PEst-C/QUI/UI0062/2013) and LSRE/LCM (pro-ject PEst-C/EQB/LA0020/2013). M. Taha acknowledges FCT for the post-doctoral grants SFRH/BPD/78441/2011.

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