In their comment, Bogdan and Loerting1 (hereafter called BoLo) question the validity of the experimental data of Lienhard et al.2 (hereafter called LZZKP) concerning the glass transition temperatures (Tg) of binary aqueous citric acid and aqueous malonic acid solutions. BoLo present own measurements and find disagreements between their results and the results published by LZZKP. In this reply, we show calorimetric thermograms from which the results published by LZZKP are derived and discuss why BoLo's criticisms are unjustified. Below, we address each of the four claims.1 

(i) Mineral-oil/lanolin vs. halocarbon-oil/lanolin as emulsion matrix: BoLo question the validity of the emulsion data reported in LZZKP because the mineral-oil/lanolin (mineral-oil CAS number 8042-47-5) mixture which is used forms itself a glass around 177 K, here referred to as

$T_\mathrm{g}^\mathrm{m}$
Tgm⁠. The mineral-oil/lanolin mixture was used by LZZKP because of the high reproducibility experienced in previous studies.3–5 Indeed,
$T_\mathrm{g}^\mathrm{m}$
Tgm
appears in each emulsion experiment at ∼177 K, but this matrix glass transition can easily be distinguished from the glass transition of the emulsified aqueous droplets. The heating cycles shown in Fig. 1(a) for emulsified aqueous malonic acid droplets clearly reveal the two distinct glass transitions. The experiment with a malonic acid weight fraction (w2) of 0.565 shows crystallization upon warming, the thermal signature of which superimposes the glass transition of the mineral-oil/lanolin matrix. We further show the heating cycles of emulsified aqueous NH4HSO4 droplets reported in Ref. 5, which were also used by LZZKP in Fig. 1(b).

The emulsion experiment with a citric acid weight fraction of 0.550 in Fig. 1(c) shows only one glass transition upon cooling, although both the mineral-oil/lanolin matrix and the aqueous droplets vitrify. The reverse transition (glass to supercooled liquid) occurs in the heating cycle followed by cold crystallization and was interpreted as Tg of the aqueous droplets, which in this experiment coincides with

$T_\mathrm{g}^\mathrm{m}$
Tgm⁠. We note that this Tg is in good agreement with the predicted Tg based on our bulk measurements.

BoLo's emulsion measurements with a halocarbon-oil/lanolin matrix and their bulk measurements yield a Tg which is 3 K lower than ours, which is not surprising as Tg depends on the cooling rate of the experiment, with larger cooling rates leading to higher Tg.6 They used a cooling rate of 3 K/min, whereas we applied the widely used cooling rate of 10 K/min.7 One order of magnitude reduction in the cooling rate typically lowers Tg by 3–5 K.8 In fact, when this difference is taken into account, the bulk measurements of BoLo agree with those from LZZKP within the experimental uncertainty. This interpretation of BoLo's results reduces the inconsistencies to a single experiment, namely, the one with aqueous droplets containing a citric acid weight fraction of 0.6 embedded in a mineral-oil/lanolin. However, we believe that the Tg-curve in Fig. 1 of LZZKP, which is based on a series of unambiguous bulk measurements, is much more convincing than this single experiment of BoLo. For comparison, we included BoLo's measurements in the phase diagram of the citric acid-water system (see supplementary material18).

FIG. 1.

Calorimetric thermograms of bulk and emulsified aqueous solutions containing (a) malonic acid, (b) NH4HSO4, and (c) citric acid, which are exemplary for the data reported by LZZKP (citric acid and malonic acid) and Zobrist et al.5 (NH4HSO4). Concentrations and technique (bulk or emulsion) are indicated. The tilted dashed-dotted line in panel (c) truncates the freezing peak to fit the figure. The scale bars represent heat flow through samples. The dotted line in panel (c) shows the warming cycle of the mineral-oil/lanolin mixture in the absence emulsified droplets.

FIG. 1.

Calorimetric thermograms of bulk and emulsified aqueous solutions containing (a) malonic acid, (b) NH4HSO4, and (c) citric acid, which are exemplary for the data reported by LZZKP (citric acid and malonic acid) and Zobrist et al.5 (NH4HSO4). Concentrations and technique (bulk or emulsion) are indicated. The tilted dashed-dotted line in panel (c) truncates the freezing peak to fit the figure. The scale bars represent heat flow through samples. The dotted line in panel (c) shows the warming cycle of the mineral-oil/lanolin mixture in the absence emulsified droplets.

Close modal

(ii) Assignment of

$T_\mathrm{g}^{{\prime }}$
Tg⁠: BoLo raise doubt about the glass transition temperature of the freeze-concentrated citric acid solution,
$T_\mathrm{g}^{{\prime }}$
Tg
, reported by LZZKP. They suspect that the reported
$T_\mathrm{g}^{{\prime }}$
Tg
(for which the uncertainty is higher than for Tg because the change in the heat flow due to this transition is weak) were confused with the signal from the termination of ice crystallization in the heating cycle. However, such a termination of ice crystallization in the heating cycle implies that the same crystallization must have been kinetically hindered in the cooling cycle. This kinetic limitation is conceivable but unexpected in emulsion experiments because the distance that the water molecules need to travel in the emulsified aqueous droplets is very small. It is therefore not surprising that our results agree with values found by Lu and Zografi9 who investigated annealed samples in a procedure recommended for the determination of
$T_\mathrm{g}^{{\prime }}$
Tg
.10 In agreement with the study of Lu and Zografi,9 we found two heat flow discontinuities upon heating,
$T_\mathrm{g1}^{{\prime }}$
Tg1
and
$T_\mathrm{g2}^{{\prime }}$
Tg2
, shown in the inset of Fig. 1(c). The higher one (
$T_\mathrm{g2}^{{\prime }}$
Tg2
) was assigned to the actual
$T_\mathrm{g}^{{\prime }}$
Tg
, while the lower (
$T_\mathrm{g1}^{{\prime }}$
Tg1
) was interpreted as the glass transition of droplets where ice did not reach equilibrium size.9 However, there are different interpretations of such discontinuities upon heating.11–15 It is possible that
$T_\mathrm{g1}^{{\prime }}$
Tg1
is the actual
$T_\mathrm{g}^{{\prime }}$
Tg
, and
$T_\mathrm{g2}^{{\prime }}$
Tg2
corresponds to the onset point of melting, usually referred to as
$T_\mathrm{m}^{{\prime }}$
Tm
.14,15 We do agree with BoLo that there is uncertainty concerning this attribution. However, we would like to underline that the value of
$T_\mathrm{g}^{{\prime }}$
Tg
is irrelevant for the conclusions drawn by LZZKP.

(iii) Experimental procedure: BoLo report that they could not reproduce the Tg of bulk aqueous citric acid solutions with citric acid weight fractions of 0.70 and 0.75. When we prepared these solutions, we took care that no impurities that may provide surfaces for heterogeneous nucleation entered the vial during the preparation. For the same reason, we did not use stir bars and held the temperature of the solution above its solubility for some time to ensure that no undissolved citric acid crystals invisible to the eye were left in the solution. It is not unusual that aqueous solutions can be supercooled with respect to the solid phase of the solute. Both Refs. 9 and 16 observed Tg of aqueous citric acid solutions with w2 > 0.70. The calorimetric thermograms of the relevant aqueous citric acid solutions observed from both bulk and emulsified samples reported by LZZKP are displayed in Fig. 1(c).

The same procedure was applied for the aqueous malonic acid solutions. Additionally, as described by LZZKP, the emulsified aqueous malonic acid droplets with w2 = 0.750 were heated to the melting temperature of pure malonic acid after Tg was observed, to make sure that no crystal was formed in the cooling cycle (not shown).

(iv) Uncertainty of

$\Delta S_\mathrm{mix}^\mathrm{l}-\Delta S_{\mathrm{mix}}^\mathrm{g}$
ΔS mix lΔS mix g⁠: BoLo dispute the choice of
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
and criticize the absence of an uncertainty estimation for
$\Delta S_\mathrm{mix}^\mathrm{l}-\Delta S_{\mathrm{mix}}^\mathrm{g}$
ΔS mix lΔS mix g
. First, we would like to clarify that
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
denotes the heat capacity difference between liquid and the glassy state of water at Tg = 136 K of pure water. As pure water undergoes a fragile-to-strong transition, which is suppressed in the presence of a solute, the value of
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
depends on how pronounced this conversion is, even when the solute is absent at w2 = 0. Therefore,
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
needs to be evaluated for each solute individually, as shown by LZZKP. We believe that the description provided by LZZKP and the references cited therein15,17 fully justify the procedure. Second, as a consequence of Eq. (12) of LZZKP, the value of
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
only scales the value of
$\Delta S_\mathrm{mix}^\mathrm{l}-\Delta S_{\mathrm{mix}}^\mathrm{g}$
ΔS mix lΔS mix g
for each individual solute, but has no effect on the relative quantities between the different solute concentrations. Regardless of the uncertainty in
$c_1^\mathrm{l}-c_1^\mathrm{g}$
c1lc1g
, which ranges from 12 to 35 J K−1 mol−1,
$\Delta S_\mathrm{mix}^\mathrm{l}-\Delta S_{\mathrm{mix}}^\mathrm{g}$
ΔS mix lΔS mix g
must adopt non-zero values. This is why no error bars are provided for
$\Delta S_\mathrm{mix}^\mathrm{l}-\Delta S_{\mathrm{mix}}^\mathrm{g}$
ΔS mix lΔS mix g
.

(v) Classification of the glass transition: In addition to points (i) to (iv), BoLo state that the entropy excess discontinuities found by LZZKP imply that the glass transition is a first order transition. However, our work does not warrant such a conclusion. The data and evaluation with regard to the excess entropy discontinuity suggest only that the glass transition is not a classical second order phase transition according to the Ehrenfest classification. Additionally, the shape of the heat flow curves at the glass transition indicates that the transition is not a first order transition. Note that the glass transition occurs between two metastable states (supercooled liquid to amorphous solid) and is at least partially a dynamic phenomenon, hence the transition temperature depends on the cooling rate.6 Therefore, it is not a purely thermodynamically controlled phase transition, which complicates the classification according to Ehrenfest.

To summarize, we thank BoLo for a series of new measurements, which, as far as the conclusions of LZZKP are concerned, corroborate our findings. The ETH Research Grant ETH-0210-1 is acknowledged.

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See supplementary material at http://dx.doi.org/10.1063/1.4812930 for phase diagram of the citric acid-water system as a function of the citric acid weight fraction as in LZZKP.

Supplementary Material