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M.V. Ol’khovich et al. / Thermochimica Acta 569 (2013) 61–65
(4-methoxy-phenyl)-(1-Thia-3-aza-spiro[5.5]undec-2-en-2-
yl)-amine (2); and 1-[4-(1-Thia-3-aza-spiro[5.5]undec-2-
synthesized by reaction of the appropriate isothiocyanate with
intermediate thiourea under acidic conditions in the final bicyclic
product [11]. The structure and purity of studied compounds
has been characterized by 1H NMR spectroscopy and elemental
analysis [10]. Purity of the spiro-derivates was 0.98 (mass fraction).
Fig. 1. Molecular structure of bicyclo-derivatives of 1,3-thiazine.
2.2. Apparatus and procedure
Temperatures and enthalpies of fusion of the compounds under
investigation have been determined using a Perkin-Elmer Pyris
1 DSC differential scanning calorimeter (Perkin-Elmer Analytical
Instruments, Norwalk, CT, USA) with Pyris software for Win-
dows NT. DSC runs were performed in an atmosphere of flowing
20 cm3 min−1 dry helium gas of high purity 0.99996 (mass frac-
tion) using standard aluminum sample pans and a heating rate of
2 K min−1. The accuracy of weight measurements was 0.005 mg.
The DSC was calibrated with an indium sample from Perkin-Elmer
(P/N 0319-0033). The value determined for the enthalpy of fusion
corresponded to 28.48 J g−1 (reference value 28.45 J g−1). The fusion
temperature was 429.5 0.1 K (determined from at least ten mea-
surements). The enthalpy of fusion at 298 K was calculated by the
following equation [12]:
identified. Under this flow rate, the saturated vapor pressure is
independent of the flow rate and, thus, thermodynamic equilibrium
is realized.
The saturated vapor pressures were measured five times at each
temperature with the standard deviation no more than 5%. Because
the saturated vapor pressure of the compounds investigated is low,
it may be assumed that the heat capacity change of the vapor with
temperature is so small that it can be neglected. The experimentally
determined vapor pressure data may be described in the following
way:
B
ln(p) = A +
(2)
T
The value of the sublimation enthalpy is calculated by the
Clausius–Clapeyron equation:
ꢀlcrHm◦ (298.15) = ꢀlcrHm◦ (Tfus) − ꢀlcrSm◦ (Tfus)(Tfus − 298.15)
(1)
ꢀ
ꢁ
∂(ln p)
∂(1/T)
ꢀgcrHm◦ (T) = −R
(3)
where the difference between the heat capacities of the melt and
solid states was approximated by the fusion entropy (as an upper
estimate).
whereas the sublimation entropy at the given temperature T was
calculated from the following relation:
Sublimation experiments were carried out by the transport
method. This method consists in passing a stream of an inert gas
over a sample at the constant flow rate and temperature, the rate
being low enough to practically achieve saturation of the carrier gas
with the substance’s vapor. The vapor was condensed and the subli-
mated quantity determined. The vapor pressure over the sample at
this temperature can be calculated from the amount of sublimated
material and the volume of the inert gas used.
(ꢀcgrH◦ (T) − ꢀgcrGm◦ (T))
ꢀgcrSm◦ (T) =
(4)
m
T
with ꢀgcrGm◦ (T) = −RT ln(p/p0), where p0 is the standard pressure
of p0 = 1.013 × 105 Pa.
For experimental reasons sublimation data are obtained at
elevated temperatures. However, in comparison with effusion
methods, the temperatures are much lower, which makes extrap-
olation to room conditions easier. In order to further improve the
extrapolation to room conditions, we estimated the heat capacities
Details of the technique are given in the literature [13]. The inert
gas (nitrogen) from tank flows through a column packed with sil-
ica to adsorb any water from the gas. The stabilization of the gas
temperature occurs in a thermostated water bath. The stability of
the gas flow with precision better than 0.01% is realized by use of
mass flow controller MKS type 1259CC-00050SU. The inert gas of
constant temperature and velocity passes then to the glass tube,
which is placed in the air thermostat. Three zones of the glass tube
can be distinguished to starting zone for stabilizing of the inert gas;
the transitional zone in which sublimation process occurs; ensuring
slow sublimation of the substance investigated; the finishing zone
in which the inert gas together with the sublimated substance is
overheated by 4–5 K, controlled by platinum resistance thermome-
ter. The temperature of the air thermostat is kept constant with a
precision of 0.01 K by means of the temperature controller PID type
650 H UNIPAN equipped with a resistance thermometer. The fin-
ishing zone is coupled with the condenser built from glass helix,
placed (outside the thermostat) located in a Dewar vessel filled
with a liquid nitrogen. To avoid a humidity adsorption from the air,
a condenser is connected to a vessel filled with CaCl2.
(
crCp◦,m-value) of the crystals using the additive scheme proposed
by Chickos and Acree [15]. Heat capacity was introduced as a cor-
rection for the recalculation of the sublimation enthalpy ꢀgcrHm◦
according to the equation:
ꢀgcrHm◦ (298.15) = ꢀgcrHm◦ (T) + ꢀHcor = ꢀcgrHm◦ (T)
+ (0.75 + 0.15crCp◦,m) · (T − 298.15)
(5)
3. Results and discussion
various bicyclo-derivatives of 1,3-thiazines. The general central
fragment of molecules is given in Fig. 1. Structural formula of radi-
cals and some of the physicochemical parameters of the substances
are shown in Table 1. All investigated compounds have a common
central fragment and various substituents with a phenyl ring and
methoxy- and carbonyl-groups in their structure.
The temperatures and enthalpies of fusion of spiro-derivatives
have been measured by DSC (Table 1). Only fusion peaks are regis-
tered on DSC curves, indicating stability and the absence of phase
transitions of the substances in the temperature ranges studied. The
experimental enthalpies of fusion increase from the first substance
The equipment was calibrated using benzoic acid. The standard
value of the sublimation enthalpy obtained was ꢀgcrHm◦ = 90.5
0.3 kJ mol−1. This is in good agreement with the value recom-
mended by IUPAC (ꢀgcrHm◦ = 89.7 0.5 kJ mol−1) [14].
From the experimentally determined pressure–flow rate rela-
tionship, the optimal flow rate of 1.2–1.8 dm3 h−1 has been