The authors have provided responses to the questions, comments and issues pointed out by both referees. They have carried out additional calculations and have modified the manuscript to account for suggested changes, where applicable.
For this second round of reviews of this technical note, I will focus on the replies and manuscript sections with changes. Most of the issues raised in the first round have been addressed well. I have found a few issues to be further addressed before this manuscript is finalized for publication.
The line numbers used in the following comments are those from the revised manuscript (ms version 3).
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\item line 300: Regarding the acid dissociation reaction (R2) notation for oxalic acid, it is a bit odd that you write the reaction using HA for the acid, given that oxalic acid is a diacid. It would be better to write the reaction as $\chem{H_2A} + \chem{H_2O} = \chem{HA^-} + \chem{H_3O^+}$ and perhaps also list the second dissociation reaction involving \chem{HA^-} (even if not considered by COSMO-RS-DARE). Further along these lines, from the main text alone it remains unclear whether both acid dissociation reactions were considered in the model or not; should be clarified.
\item section 3.2.2, line 282 and Supplement, Fig. S3 -- S5: The experimental data shown in these figures and related interpretation in the text needs to be corrected.
For example, in Fig. S3, 'growth' mode data from EDB experiments by Peng et al. (2001) and Choi and Chan (2002) are shown. At higher acid concentrations, under growth conditions (also listed as 'condensation' for Peng et al data), dicarboxylic acids are mostly in the effloresced/crystalline state. The measurement data do not reflect aqueous solutions and cannot be used to derive water activity coefficients. It seems the authors used those data points as if they were showing values for a single aqueous solution, which is clearly incorrect. Showing such growth data is confusing and pointless for the comparison in these figures.
Have a look at Fig. 8 from Choi and Chan (2002). It is clear from that figure that any EDB growth mode data for $a_w < 0.83$ is for the effloresced glutaric acid case, for which the aqueous phase composition, if present, is simply unknown from these measurements. Furthermore, any data for water activities less than about 0.3 are also indicative of efflorescence of the acid; therefore these data cannot be used to derive water activity coefficients. For reference, at a water activity of $\sim$~0.4, the mass fraction of solute (mfs in the Fig. 8 of Choi and Chan) is about 0.9, which corresponds to about $x_{acid}$ of 0.55 for the 'evaporation' data points. The water activity coefficient there is about 0.89 (convention I). There is no (valid) water activity coefficient data in purely aqueous solution of glutaric acid that would suggest water activity coefficients to increase substantially at high $x_{acid}$ (say for $x_{acid} > 0.6$). Therefore, the experimental data shown in Fig. S3 (and similarly in S4, S5) need to be corrected (no growth / condensation data fro EDB measurements should be shown, nor the evaporation branch data for low water activity < ~0.3, depending on the acid). The related discussion in the main text and supplement needs to be corrected as there is no measurement data supporting an increase in water activity coefficient to large values at high $x_{acid}$ for the diacids. In Fig. S3d, the shown COSMO-RS, Acid dimer variant, UNIFAC and AIOMFAC model curves are likely showing the correct trend towards high acid fraction.
\item section 3.2.2, line 287: Correct the sentence; "supersaturated" and "crystalline" have different meaning and the phrasing here confuses this. An acid solution cannot be supersaturated and "crystalline" at the same time; in the presence of a crystalline phase, the remaining aqueous solution will automatically be saturated under equilibrium conditions (but not to be confused with the composition at the solubility limit).
\item Abstract, line 8: correct phrasing: "fitting parameters" should be "use of fit parameters". Also, this sentence would make more sense if it were stated for what purpose the fit parameters were introduced. Of course, with a sufficient number of fit parameters and associated functions, one could use all kinds of models to fit thermodynamic data.
\item line 89: Rephrase the following: "Pseudo-chemical potential has recently been used in molecular level solvation thermodynamics as a replacement to chemical potential". "replacement" is not a good description since the pseudo-chemical potential is not replacing the meaning or use of the chemical potential in thermodynamics; it simply expresses a different quantity, which is why naming it "pseudo-chemical" remains an unfortunate choice by Ben-Naim.
\item line 98 and Eq. (4): This sentence is unclear: "In LLE, the standard chemical potential ($\mu$) of a compound is equal in both of the liquid phases..." and also on line 101: "The standard chemical potential of compound $i$ in a solution is defined using the standard chemical potential at the reference state.". In both sentences, the authors seem to confuse the chemical potential with the term "standard chemical potential" -- they are equivalent. The word "standard" has very specific meaning in thermodynamics and should not be confused with "regular" or "usual". In the second sentence, it should be "The standard chemical potential of compound $i$ in a solution is defined using the chemical potential at the reference state" (where, in convention I, the second term on the right hand side vanishes).
\item line 106, Eq. (6): The notation of this equation is wrong. The phase should be specified for each activity (e.g. as superscript; $a_i^\alpha$) since that is the point of the isoactivity condition among different phases. The same should also be corrected for Eq. (4). It is also potentially misleading to state the mole fraction in parenthesis, because this equation could be misunderstood as activity times mole fraction = ...
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