Thermodynamic properties of caffeine: reconciliation of available experimental data
J. Chem. Thermodynamics 40 (2008) 1661–1665
Thermodynamic properties of caffeine: Reconciliation of availableexperimental data
Vladimir N. Emel’yanenko, Sergey P. Verevkin *
Department of Physical Chemistry, University of Rostock, Hermannstrasse 14, D-18051 Rostock, Germany
Molar enthalpies of sublimation of two crystal forms of caffeine were obtained from the temperature
dependence of the vapour pressure measured by the transpiration method. A large number of primary
experimental results on the temperature dependences of vapour pressure and phase transitions have
been collected from the literature and have been treated in a uniform manner in order to derive sublima-
tion enthalpies of caffeine at T = 298.15 K. This collection together with the new experimental resultsreported here has helped to resolve contradictions in the available sublimation enthalpies data and to
recommend a consistent and reliable set of sublimation and formation enthalpies for both crystal forms
under study. Ab initio calculations of the gaseous molar enthalpy of formation of caffeine have been per-
formed using the G3MP2 method and the results are in excellent agreement with the selected experi-
Ó 2008 Elsevier Ltd. All rights reserved.
the help of additional experimental measurements. Additionalsupport for the measured values comes from ab initio calculations
We have commenced studies on the thermochemical proper-
of gaseous molar enthalpy of formation of caffeine using the
ties of purine-like compounds with the aim of enlarging insight
into the energetics of nucleic acids. Caffeine is a compound ofconsiderable industrial and environmental significance. Caffeine
is a relatively simple model compound, which is useful in under-standing the structure–energy relationships of nucleic acids. Ther-
modynamic properties of caffeine have been extensively studied. However, thermochemical data on caffeine are in apparent
A sample of anhydrous caffeine obtained as the a-phase mate-
disarray (see A very careful thermochemical study (com-
rial (CAS registry number 58-08-2) was obtained from Sigma
bustion calorimetry and DSC) of two anhydrous polymorphs of
(USP grade). It was further purified by fractional sublimation at
caffeine has been recently published in this journal Several
T = 383 K and at reduced pressure. The purity analyses were per-
months later, another thermochemical study of caffeine ap-
formed using a gas chromatograph (GC) with a flame ionisation
peared in the same journal, where the reported combustion en-
detector. A HP-5 capillary column (stationary phase cross-linked
thalpy of the a-phase of caffeine differs by about 20 kJ Á molÀ1.
5% PH ME silicone) was used in all our experiments. The column
Since 1979, vapour pressure and enthalpies of sublimation of caf-
was 30 m long, had an inside diameter of 0.32 mm , and a film
feine polymorphs have been measured using diverse methods.
thickness of 0.25 lm. The flow rate of the carrier gas (nitrogen)
We have carefully collected the primary experimental results on
was maintained at 7.2 dm3 Á hÀ1. The starting temperature for
the temperature dependence of vapour pressure and phase transi-
the GC was 323 K for the first 180 s, followed by heating to
tions available in the literature (see ). Analy-
T = 523 K at the rate of 10 K Á minÀ1. No impurities greater than
sis of the primary experimental data reveals that the sublimation
0.02 mass per cent were detected in the sample used in this
enthalpies of the caffeine spread over 11 kJ Á molÀ1 for the a-poly-
morph, and over 4 kJ Á molÀ1 for the b-polymorph. The purpose ofthis paper is to resolve the existing disagreement between the
2.2. Vapour pressure measurements of caffeine
available values of the sublimation enthalpies of caffeine, with
Vapour pressure and enthalpies of sublimation, Dg H
feine polymorphs were determined using the method of transpira-
* Corresponding author. Tel.: +49 381 498 6508; fax: +49 381 498 6502.
tion in a saturated nitrogen stream. About 0.5 g of the sample
0021-9614/$ - see front matter Ó 2008 Elsevier Ltd. All rights reserved. doi:10.1016/j.jct.2008.07.002
V.N. Emel’yanenko, S.P. Verevkin / J. Chem. Thermodynamics 40 (2008) 1661–1665
Compilation of data on enthalpies of sublimation Dg H
Standard ab initio molecular orbital calculations were per-
formed with the Gaussian 03 Rev. 04 series of programs . Ener-
gies were obtained at the G3MP2 level of theory. The G3 theory is a
procedure for calculating the energies of molecules containing
atoms of the first and second rows of the periodic chart based on
ab initio molecular orbital theory. A modification of G3 theory that
uses reduced orders of Moller–Plesset perturbation theory is the
G3(MP2) theory This method saves considerable computa-
tional time compared to G3 theory with some loss in accuracy, but
is much more accurate than G2MP2 theory. For all the species in-cluded in this study, full geometry optimisations were carried
out at the HF/6-31G(d) level. The corresponding harmonic vibra-
tional frequencies were evaluated at the same level of theory to
Vapour pressures available in the literature were treated using equations
confirm that the optimised structures found correspond to the po-
in order to evaluate enthalpy of vaporization at T = 298.15 K, in the same way asour own results in
tential energy minima and to allow the evaluation of the corre-sponding zero-point vibrational energies, ZPE, and the thermalcorrections at T = 298 K. The ZPE values were scaled by the empir-
ical factor 0.8929. All the minima found at the HF/6-31G(d) level
Compilation of the data available for the solid phase transition, DtransHm, and the
were again fully re-optimised at the MP2(FULL)/6-31G(d) level.
The G3MP2 theory uses geometries from second-order perturba-
tion theory and scaled zero-point energies from Hartry–Fock the-
ory followed by a series of single-point energy calculations at the
MP2(Full), QCISD(T), and MP2/GTMP2Large levels of theory (for
details see reference The enthalpy value of the compound
studied at T = 298 K was evaluated according to the standard ther-
Caffeine was found to display a low-temperature a-polymorph
modification at room temperature with the trigonal crystal struc-
a Techniques: DTA, Du Pont 990 Thermal Analyzer; MCB, differential heat flux
ture At T = 414 K, the a-polymorph of caffeine transforms into
calorimeter MCB; TE, torsion effusion method; DSC, differential scanning calorim-
a b-crystal phase and remains in this phase until the melting
etry; SC, solution calorimetry; CC, combustion calorimetry; T, transpiration. b
Taken into account for the calculation of the average enthalpy of the phase
transition (3.8 ± 0.3) kJ.molÀ1. c Average enthalpy of fusion (21.4 ± 0.6) kJ Á molÀ1 was calculated from the data
3.1. Vapour pressure and sublimation enthalpies
Vapour pressures of caffeine polymorphs measured in this work
and those from the literature were treated with equations
was mixed with glass beads and placed in a thermostated
U-shaped tube having a length of 20 cm and a diameter of
0.5 cm. Glass beads with a diameter of 1 mm provide a surface
large enough for rapid (vapour + solid) equilibration. At constant
temperature (±0.1 K), a nitrogen stream was passed through the
U-tube and the transported amount of material was collected in
p , required for the correction of the sublima-
a cooling trap. The flow rate of the nitrogen stream was measured
tion enthalpies, have been derived according to a procedure devel-
using a soap bubble flow meter and was optimised in order to
oped by Chickos and Acree The following values: Dg C
reach the saturation equilibrium of the transporting gas at each
temperature under study. The transported material was collected
40:8 J Á KÀ1 Á molÀ1 for the b-phase have been used in this
in a special cold trap and the amount of condensed product was
p ¼ 95:3 J Á KÀ1 Á molÀ1, required for adjust-
determined by weighing (±0.0001 g). The saturation vapour pres-
ing the vaporization enthalpy (see was calculated using
the group contribution method of Chickos and Acree . In order
of the product collected within a definite period of time. Assuming
to assess the uncertainty of the sublimation enthalpy, the experi-
that Dalton’s law of partial pressures applied to the nitrogen
mental data were approximated with the linear equation
stream saturated with the substance i of interest is valid, values
lnðpsatÞ ¼ f ðTÀ1Þ using the method of least squares. The uncertainty
of psat were calculated using the equation
in the enthalpy of sublimation was assumed to be identical with
the average deviation of the experimental lnðpsatÞ values from this
linear correlation. The experimental results for sublimation enthal-
where R = 8.314472 J Á KÀ1 Á molÀ1, mi is the mass of the transported
pies, and parameters a and b according to equation are listed in
compound, Mi is the molar mass of the compound, and Vi is its vol-
In order to ensure complete phase conversion to the
ume contribution to the gaseous phase. VN2 is the volume of the car-
b-phase during the transpiration measurements, the sample was
rier gas and Ta is the temperature of the soap bubble meter. The
firstly heated to T = 434.5 K and was kept at this temperature for
volume of the carrier gas, VN2, was determined from the flow rate
about 30 min. The vapour pressure experiments were conse-
quently done from the higher to lower temperatures.
V.N. Emel’yanenko, S.P. Verevkin / J. Chem. Thermodynamics 40 (2008) 1661–1665
m ð298:15 KÞ ¼ ð108:1 Æ 1:1Þ=ðkJ Á molÀ1 Þ
lnðp=PaÞ ¼ 307:56 À 116102:54 Á ðT=KÞ À 26:8 ln
m ð298:15 KÞ ¼ ð104:2 Æ 3:6Þ=ðkJ Á molÀ1 Þ
lnðp=PaÞ ¼ 313:26 À 116335:98 Á ðT=KÞ À 40:8 ln
a Temperature of saturation. b Mass of transferred sample, condensed at T = 293 K. c Volume of nitrogen, used to transfer the mass m of the sample. d Vapour pressure at temperature T, calculated from m and the residual vapour pressure at T= 293 K.
The temperature dependence of the vapour pressure for the so-
lid caffeine is presented in . As can be seen, our vapour
pressures are in a good agreement with the results measured bythe static method and by the Knudsen effusion method . Vapour pressures reported by Griesser et al. lie systematically
above the data available, most probably due to an error in the cal-ibration. Vapour pressures measured using the effusion method
are somewhat below the available data, however, the trend seemsto be correct.
The sublimation enthalpy of the b-phase of caffeine derived in
m ð298:15 KÞ ¼ ð104:2 Æ 3:6Þ kJ Á molÀ1, is definitely
lower than those from Griesser et al. Dg H
kJ Á molÀ1 from Bothe and Cammenga even taking into ac-
count the large uncertainty of our results. It was not possible forus to determine the sublimation enthalpy of the b-phase of caffeine
by the transpiration method more precisely, because of the very re-stricted temperature range from (420 to 434) K, which was at the
The set of available sublimation enthalpies of the a-phase of
caffeine also shows a large spread in values, from (106 to117) kJ Á molÀ1 (see ). There are two values from and
FIGURE 1. Plot of vapour pressure measurements against reciprocal temperature
from close to the level of 117 kJ Á molÀ1 and there are also
for caffeine: ‘d’ – this work; ‘s’ – a-phase ; ‘+’ – b-phase ; ‘N’ – a-phase ;‘h’ – a-phase ; ‘M’ – b-phase ; ‘j’ – liquid phase ; ‘}’ – a-phase . The
two values (and this work]) close to the level of 106 kJ Á molÀ1.
dotted lines indicate the temperatures of the phase transitions.
Which value of sublimation enthalpy is preferred?
3.2. Consistency tests of the experimental results
py of phase transition of caffeine obtained by calorimetry
Since a significant discrepancy in the available experimental
sublimation enthalpy results collected in has been found,additional arguments to support the reliability of our new mea-
As can be seen from the DSC results for the phase transition
3.2.1. Internal consistency of sublimation enthalpies and the enthalpy
DtransHm(a ? b) from different sources are very consistent and the
average value of (3.8 ± 0.3) kJ Á molÀ1 was calculated from these
A valuable test of the internal consistency of the experimental
results. Comparing the latter value with the enthalpy of phase tran-
data of sublimation enthalpies for the a- and b-phase measured
sition calculated using equation from the difference of Dg H
in this work (see is the comparison with the enthal-
(for the a and b phases) measured in this work (see ):
V.N. Emel’yanenko, S.P. Verevkin / J. Chem. Thermodynamics 40 (2008) 1661–1665
DtransHm(a ? b) = 108.1–104.2 = (3.9 ± 3.8) kJ Á molÀ1. This estimate
that has been proven to be consistent with the phase transition
does not differ from the results measured by calorimetry (see
enthalpy measured by DSC (see ). The values are in close
). Hence, in this way, our results for the sublimation enthalpies of
agreement with the value DtransHm(a ? b) = (2.0 ± 0.3) kJ Á molÀ1,
the a- and b-phase seem to be consistent. Similar treatment of
measured using a solution calorimeter . Surprisingly, the
the sublimations enthalpies measured by Bothe and Cammenga
most recent value, Df H ðcrÞ ¼ ðÀ322:2 Æ 4:8Þ kJ Á molÀ1 for the
a-phase of caffeine measured by Dong et al. by using
(5.2 ± 0.9) kJ Á molÀ1 and those from Griesser et al. : Dtrans
macro-combustion calorimetry is about 20 kJ Á molÀ1 less negative
Hm(a ? b) = 116.6–108.5 = (8.1 ± 0.5) kJ Á molÀ1. Our results as well
than the results from Pinto and Diogo . We do not have any
as those from Bothe and Cammenga are internally consistent;
disagreement between these data sets remains apparent.
sample by Dong et al. was contaminated with the b-phase, thedisagreement could be only within (2 to 5) kJ Á molÀ1 as shown
3.2.2. Internal consistency of sublimation enthalpies adjusted to the
above. We shall try to resolve this contradiction with the help of
our new values of sublimation enthalpies and high-level ab initio
An additional argument to support the experimental results
measured in this work is to consider the following thermochemicalcycle:
3.2.4. Experimental enthalpies of formation of caffeine in the gaseousphase
Values of sublimation enthalpies of caffeine, derived in this
work, have been checked for internal consistency. These values(see can now be used for further calculation of the stan-
mðT fusÞ in equation was obtained by adjusting the
enthalpy of vaporization measured by a static manometer (see
For this purpose, we selected first the enthalpies of formation
from Tav = 516.5 K to Tfus = 509 K. The value DgH
ðcrÞ of for a- and b-phase of caffeine reported by Pinto and
equation is the average of the available literature data (see
Diogo and the resulting values of the standard molar enthalpies
mðT fusÞ ¼ ð97:1 Æ 0:9Þ kJ Á molÀ1
compared with the similar adjustments of our new sublimation
modynamic properties of a-phase) and Df H ðgÞ ¼ ðÀ236:4 Æ 4:3Þ
enthalpies (according to equation for the b-phase of
kJ Á molÀ1 (from the thermodynamic properties of b-phase). The
very good agreement between these values is again further evi-dence of the internal consistency of the results selected in this
work. However, the absolute value of the gaseous enthalpy of for-
mation of caffeine still remains questionable. An additional possi-bility to test the consistency of the selected data is the
comparison of the experimental gaseous enthalpy of formation ofcaffeine with the value calculated using quantum chemical calcu-
For the adjustment of the sublimation enthalpy for the a-phase of
lations. Such a test could be performed in the manner we sug-
caffeine, the phase transition DtransHm(a ? b) = (3.8 ± 0.3) kJ Á molÀ1
at Ttrans = 414 K (see ) should be additionally taken into ac-count and it should also be adjusted to Tfus. The adjustment forthe a-phase of caffeine is as follows:
3.2.5. Enthalpy of formation of caffeine in the gaseous phase: quantumchemical calculations
The ab initio molecular orbital methods used for the calculation
p  ðT av À T fusÞ À DtransHmða ! bÞÂ
of the enthalpy of formation of caffeine have not been yet reported
in the literature. We have calculated using the G3MP2, a total en-
¼ 105:7 À 0:0268 Â ð509 À 388Þ À 3:8 þ 0:0014 Â
ergy at T = 0 K, E0 = À679.383314 Hartree and enthalpy at T =
298.15 K, H298 = À679.369094 Hartree. In standard Gaussian-n the-
ories, theoretical standard enthalpies of formation, Df H ðgÞ, are
calculated through atomization reactions . Using this proce-
As can be seen, results which have been obtained according to
dure we have obtained for caffeine Df H ðgÞ ¼ À235:5kJ Á molÀ1.
equations are in excellent agreement. This fact provides
Thus, the theoretical enthalpy of formation of caffeine is in excel-
the additional evidence for the internal consistency of the experi-
lent agreement with the experimental values derived from com-
mental results determined in this work.
bustion experiments by Pinto and Diogo and enthalpies ofsublimation measured in this work. Hence, with the help of this
3.2.3. Experimental enthalpies of formation of caffeine in the
theoretical result we are able to resolve the uncertainty in the
available thermochemical data on caffeine.
The values of enthalpies of sublimation Dg H
are required to obtain gaseous enthalpies of formation, Df H ðgÞ,
of organic compounds, provided that their enthalpies of formationin the condensed phase, Df H (cr), are known. Standard molar
This investigation was undertaken to establish a consistent set
enthalpies of formation Df H ðcrÞ ¼ ðÀ345:1 Æ 2:3Þ kJ Á molÀ1 for
of vapour pressures, sublimation, and formation enthalpies of caf-
the a-phase and Df H ðcrÞ ¼ ðÀ340:6 Æ 2:3Þ kJ Á molÀ1 for the b-
feine. We collected from the literature a large number of primary
phase of caffeine were measured by Pinto and Diogo by
experimental results and treated them uniformly in order to derive
micro-combustion calorimetry. The difference between these val-
T = 298.15 K. The data sets on phase transitions were checked for
internal consistency. This collection together with the new exper-
transHmða ! bÞ ¼ Df H ; ðcrb-phaseÞ À D
imental results and theoretical calculations reported here has
helped to resolve contradictions in the available thermochemical
V.N. Emel’yanenko, S.P. Verevkin / J. Chem. Thermodynamics 40 (2008) 1661–1665
data and to recommend consistent and reliable sublimation and
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This work has been supported by the Research Training Group
‘‘New Methods for Sustainability in Catalysis and Technique”
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