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METHOD FOR QUANTITATIVE DETERMINATION
OF VARIOUS FORMS OF WATER IN BIOLOGICALLY
ACTIVE SUBSTANCES
B. N. Boiko,1,* I. M. Kolpakov,1, 2 and A. A. Uminskii1
Translated from Khimiko-Farmatsevticheskii Zhurnal, Vol. 44, No. 10, pp. 46 – 52, October, 2010.
Original article submitted June 24, 2009.
The content of water in substances and preparations based on biologically active materials determines to a
considerable extent their biopharmaceutical properties and stability. A new method has been developed for
separate quantitative determination of water in various bound forms in biologically active substances isolated
from raw plant materials. Dihydroquercetin is used as an example to demonstrate that the proposed method is
capable of determining water fractions with various degrees of binding in a sample.
Key words: water in biological substances, quantitative determination.
Water contained in substances and preparations of biologically
active compounds determines to a considerable extent
the level of their biological activity and stability. Not
only the total water content but also its distribution among
fractions with various bond strengths to the active compound
is important. Various methods and modes of drying influence
the distribution and determine the quality of the resulting
product.
The goal of the present study was to develop a method
for separate determination of the quantitative content of water
with different bond strengths in biologically active substances
obtained from raw plant material. Dihydroquercetin
(DHQ) substance was selected as the studied sample.
Let us differentiate fractions of free water, weakly bound
water, and strongly bound water. The lack of uniform terminology
obliges us to define these concepts for the present article.
According to the common definition, free water will be
considered the fraction capable of translocation in the sample
under the influence of gravitational forces. The physical
properties of this fraction correspond fully to those of water
in condensation, evaporation, and crystallization processes.
Strongly bound water is the fraction that is called in certain
sources constitutional. We will consider it to be the fraction
released only with molecular destruction of the principal
compound, e.g., as a result of melting or thermal destruction.
Weakly bound water will be considered those fractions
for which the bond energy under normal conditions does not
permit them to translate in the sample under the influence of
gravitational forces or to be evaporated freely. However, the
increase of their internal energy due to heat absorption upon
heating destroys this bond even before the temperature of destruction
or melting is reached.
The physical nature of these fractions is different. However,
they can be classified as follows with respect to thermodynamics.
One of the principal modern experimental methods
for studying the thermodynamic properties of substances
and preparations of biologically active compounds is differential
scanning calorimetry (DSC). This method is used in
the present study.
Interpretation of thermograms
Figure 1 shows two DSC thermograms for DHQ samples
that were obtained under different experimental conditions.
Thermogram 1 was obtained at constant volume with samples
packaged in hermetic containers. Thermogram 2 was
obtained at constant pressure with samples packaged in
non-hermetic containers that allowed free exchange of gas
with the atmosphere.
The thermograms were produced with subtraction of a
baseline consisting of the sample heat capacity changes with
temperature. A spline was used to interpolate this curve under
the peak for the enthalpy change [1].
574
0091-150X/11/4410-0574 © 2011 Springer Science+Business Media, Inc.
Pharmaceutical Chemistry Journal Vol. 44, No. 10, 2011
1
Institute of Biological Instrumentation, RAS, Pushchino, Russia.
2
Pushchino State University, Pushchino, Russia.
* e-mail: [email protected];
[email protected]; [email protected]
Free and weakly bound water and traces of EtOH, which
was used in the DHQ production process [2, 3], evaporated
in both thermograms in the temperature range from the start
to 122°C. Endothermic peak A corresponds to these processes.
Exothermic peak B in the temperature range 134.8 –
148.3°C was studied before [4]. It was identified only in
samples that were not heated above 40°C during drying and
only for samples with non-hermetic packaging, i.e., under
conditions of free gas exchange with the atmosphere. We
suppose that the peak is present only in samples in which the
molecules had their native structure in the preparation and
retained it during drying. It corresponds to the energy of an
oxidation reaction involving oxygen of air. This is consistent
with the fact that this peak is missing for samples in hermetic
packaging. The presence and specific energy of this peak can
act as a quality criterion for both the DHQ preparation and
the manufacturing process.
Endothermic peak C in the rather narrow temperature
range 220 – 258°C has a high specific energy and corresponds
to DHQ melting (Table 1). The crystalline structure
of DHQ is destroyed, releasing strongly bound water [5, 6].
The last broad endothermic peak D in the range
260 – 280°C is thermal destruction of the melt and release of
gas from all destroyed DHQ constituents and certain impurities.
The goal of the present study was to determine the physical
properties of the fractions forming peak A (from 30 to
122°C).
The shape of peak Ais complicated because the temperatures
of the processes in the three fractions that it represents
overlap.
The shape of peak A obtained in thermogram 2 can be
represented as the sum of three fundamental peaks. This is
shown in Fig. 2. Peak 1 corresponds to evaporation of EtOH
distributed throughout the sample. The shape of this peak is
Gaussian for the model.
Peak 2 reflects the difference between curve A and peaks
1 and 3. Its shape is an asymmetric Gaussian curve. It correlates
well with evaporation of free water before the start of
and during boiling.
Peak 3 corresponds to evaporation of weakly bound water.
The evaporation mechanism is determined by the type
and energy of the bond. This peak also is represented well by
a Gaussian curve. These models were used in the procedure
for separating the peaks. The deviation of the curve obtained
by summing peaks 1, 2, and 3 from that of peak A on the
thermogram had a mean-square deviation of %, as will be
shown in the results.
The energy of peaks 1, 2, and 3 includes the phase-transition
energy of the fraction into the gaseous state and the work
for expansion of the resulting gas phase of this fraction. The
processes are described by equations of the first law of thermodynamics
and the Mendeleev – Clapeyron equation.
EXPERIMENTAL PART
DHQ substance of 98% purity from the bottom end of Siberian
and Daur larch that was obtained from the Laboratory
of Technology and Equipment for Complex Processing of
Raw Plant Material, IBP, RAS (Pushchino, Russia) was used
as the studied sample. The purity of the sample was confirmed
by NMR methods on an AM-300 spectrometer
(Bruker, Germany). PMR spectra were recorded in
DMSO-d
6
. Resonances in PMR spectra of DHQ in
DMSO-d
6
were assigned in the range 0.5 – 12 ppm [5].
The studies were carried out in a thermal analysis system
consisting of a differential scanning calorimeter (DSC)
(DSM-10MA, IBP, RAS), a computer, and DSMCALC applied
programs that enabled the temperatures, energies, and
areas of peaks recorded on thermograms to be determined.
Metrological characteristics of the instrument were calibrated
using certified standards for temperatures and energies
of phase transitions for naphthalene (80.28 0.2°C, 150
J/g), indium (156.45 0.2°C, 28.44 J/g), and tin
(231.75 0.3°C, 60.67 J/g) according to methodical instruc-
Method for Quantitative Determination of Various Forms 575
20 34 48 62 76 90 104 118 132 140 160 174 188 202 216 230 244 258 272 286
endo
exo
4
2
0
–2
–4
À
À Â
Ñ
Ñ
D
D
dP, mW
1
2
T, °C
Fig. 1. DSC-thermograms for hermetic and non-hermetic sample packaging.
tions MI 496–84. All thermograms for calibration and experimental
samples were recorded at scan rate 8K/min and sensitivity
range 1 for heat flux and temperature from 20 to
300°C. Weights were measured on a Sartorius R200D balance
(Germany).
The studied samples were divided into two groups:
Group 1 included samples with similar weights of
5 0.25 mg. Samples were packaged in hermetic and
non-hermetic containers;
Group 2 included samples with weights from 1 to 10 mg
in steps of 1 0.15 mg. Only samples packaged in non-hermetic
containers were studied.
All samples were sealed hermetically in aluminum containers
after weighing in order to exclude absorption of moisture
from the atmosphere before the start of the measurement.
Containers with samples intended for non-hermetic
measurement conditions were punctured immediately before
the measurement. The results were reproducible if at least
five punctures of ~0.5-mm diameter were made.
All measurements of group 1 were made in series of at
least 10 samples for each of the experimental conditions. The
series had at least 3 samples for group 2.
Some of the group 1 samples with non-hermetic packaging
were scanned up to 122°C, after which they were
weighed. The results were used to determine the total mass
loss of the sample caused by the processes in the peak:
[Equation (1), R. p. 48],
m = m
init
– m
122
, (1)
where m is the total mass loss of the sample (mg); m
init
, the
initial mass of the sample (mg), m
122
, the mass of the same
sample after scanning to 122°C (mg).
The quantity m represents the total mass of fractions
evaporated from the sample during scanning to 122°C:
m = m
1
+ m
2
+ m
3
, (2)
where m is the total mass of the fractions (mg); m
1
, the
mass of the EtOH fraction (mg); m
2
, the mass of the free water
fraction (mg); m
3
, the mass of the weakly bound water
fraction (mg).
The mass fraction
i
of each peak relative to the total
mass loss m is:
576 B. N. Boiko et al.
TABLE 1. Parameters of Group 1 Peaks for DHQ Samples with Hermetic and Non-hermetic Packaging
Parameter
Peak designation
A(1) A(2) B(1) B(2) C(1) C(2) D(1) D(2)
Melting point, °C 58.74 2 42.22 1.45 – 134.81 52* 241.409 0.11 240.09 0.67 259.89 0.54, 258.81 1.52
Peak maximum, °C 98.44 0.22 100.06 0.23 – 139.05 0.45 246.79 0.17 246.26 0.43 268.41 1.11 268.3 1.48
Specific heat of fusion,
J/g
313.77 1.51 331.52 2.24 – 28.26 2.22
31.956**
134.497 1.52 141.603 2.24
161.149**
9.32 1.22 10.818 1.8
12.03**
Note. Curve number is shown in parentheses.
*
Temperature of start of DHQ oxidation.
**
Specific heat per DHQ dry weight (initial weight from which the total amount of free and weakly bound water was subtracted).
20 26 32 38 44 50 56 62 66 74 80 86 92 96 104 110 116 122 120 134
endo
dP, mW
2
1
0
Peak 1
Peak 2
Peak 3
T, °C
Fig. 2. Peak separation in a sample with non-hermetic container packaging.
i
m
m m m
1 2 3
100%. (3)
The mass of each fraction was determined by estimating
the contribution of the fractions to the measured total energy
of peak A by separating peaks according to the aforementioned
interpretation. Considering that the energy distribution
over the fractions is proportional to the distribution of
the peak areas of these fractions on the thermogram, we obtain:
Q
QS
S
i
i , (4)
where Q is the total energy of peak A (mJ); S, the total area
of peak A (area units); Q
i
, the energy of processes for fraction
i (mJ); S
i
, the peak area of fraction i (area units).
The mass of the EtOH fraction was calculated using its
known specific heat of vaporization [7]. The small values of
the relative temperature change in the examined EtOH evaporation
process enable this process to be considered not only
isobaric but also isothermal. The effect of the uncertainty of
this assumption on the resulting estimates is small because
the mass fraction of the determined fraction is small. Joint
solution of the Mendeleev—Clapeyron equation and the first
law of thermodynamics with respect to the mass gives:
m
Q
q
RT
M
1
1
1
, (5)
where m
1
is the mass fraction of EtOH (mg); Q
1
, the vaporization
energy of the EtOH fraction (mJ); q
1
, the molar vaporization
energy of the EtOH fraction (4.81 106 mJ/mol);
R, the molar gas constant [8310 mJ/(mol·K)]; M, the molar
mass of the EtOH fraction (46,069 mg/mol); T, the average
temperature of the process (K).
For the free water fraction, the temperature change and
dependence of specific heat of vaporization on temperature,
which is described by the empirical formula Eq. (6) [8],
should be taken into account:
q
2
(t ) = (25 – 0.024t ) 103, (6)
where q
2
(t) is the specific heat of vaporization of the free water
fraction (mJ/mg); t, the temperature at which the free water
fraction evaporates (°C).
Method for Quantitative Determination of Various Forms 577
TABLE 2. Physical Properties of Fractions Forming Peak A
Peak
Parameter
Qi, mJ qi, J/g
i, % Mole H2O/mole DHQ
1 91.339 839.9* 0.246 0.014 0.018**
2 946.173 varies from 2400 to 2269 using
Eq. 6
9.428 0.31 0.911
3 455.365 3766.486 14.11 2.711 0.171 0.523
*
Handbook value.
**
Mole C
2
H
5
OH (peak 1 corresponds to evaporation of EtOH); i, peak number.
20 34 48 62 76 90 104 118 132 146 160 174 188 202 216 230 244 258 272 286
endo
exo
4
2
0
–2
–4
À
À Â
Ñ
Ñ
D
D
dP, mW
1
2
T, °C
Fig. 3. DSC-thermograms of group 1 samples with hermetic and non-hermetic packaging.
Therefore, Eq. (5) is valid for the small range of temperature
changes in which the process can be considered to be
isothermal with the specific heat of vaporization corresponding
to this temperature. Taking into account the work of vapor
expansion for this range, we obtain:
m
dQ
q t
R t
M
2
2
2
27315
( )
( . )
, (7)
where m
2
is the mass fraction of evaporated free water due to
energy dQ at temperature t (mg); dQ
2
, the absorbed energy of
the free water fraction at temperature t (mJ); R, the molar gas
constant [8310 mJ/(mol·K)]; M, the molar mass of the free
water fraction (18,000 mg/mol).
The mass fraction of free water dm
2
was estimated by
numerical integration of Eq. (6). Taking into account the
work of vapor expansion gives a correction of the order of
0.03 mg for the mass of evaporated water (0.4 mg).
We determine the mass of weakly bound water from the
resulting values m
1
and m
2
according to Eq. (1):
m
3
= m – m
1
– m
2
. (8)
Two parameters for the weakly bound water fraction are
interesting. These are the molar mass relative to the molar
mass of DHQ, which indicates the amount of water bound to
578 B. N. Boiko et al.
minit = 10,05 mg
m = 9,02 init mg
m = 8,41 init mg
m = 7,13 init mg
m = 6,14 init mg
m = 3,91 init mg
m = 4,95 init mg
m = 3,19 init mg
m = 1,03 init mg
m = 1,97 init mg
endo
exo
dP, ìÂò
6
4
2
0
Peak 1
Peak 2
Peak 3
20 26 32 38 44 50 56 62 66 74 80 86 92 98 104 110 116 122 128 134 T, °C
Fig. 4. Separation of fractions forming peak A for group 2 samples with variable weight.
one DHQ molecule, and the specific energy of vaporization,
which enables the bond energy of this fraction to be estimated.
In order to determine the specific energy of vaporization
of weakly bound water, we subtract from energy Q
3
the work
for expansion of the formed vapor corresponding to mass m
3
at the mean temperature of the peak:
Am
m RT
M
3
3 , (9)
where R and M are the same as for Eq. (5) and T is the average
temperature for peak 3 (373 K).
We obtain:
q
Q A
m
m
3
3
3
3
( )
(10)
RESULTS AND DISCUSSION
The study of the water content in initial group 1 samples
(Fig. 3) showed that DHQ contains 11.91% total water fractions.
That amount exceeds the norm indicated in the
pharmacopoeial article FS 42-3853-99 and SP XI (less than
7%).
Table 2 presents results from the determination of the
thermophysical parameters of DHQ group 1 samples.
The above measurements for DHQ group 1 samples
showed that the fractions forming peak A can be divided into
fractions belonging to EtOH and free and weakly bound water,
as was shown in Fig. 2.
Endothermic peak 1 in the temperature range 46 – 82°C
represents energy losses to evaporation. It is identified as
EtOH with a maximum near 63°C that is shifted to lower
temperature relative to the handbook boiling point of 78°C.
This is probably a result of the fact that EtOH manages to
evaporate before the start of boiling and is present as an impurity
in large amounts of water and DHQ. DSC and NMR
data for the quantitative content of EtOH showed about 0.3
and 0.5 mass %. The quantitative content of EtOH can be determined
more accurately by DSC methods if it is considered
that the vaporization energy of this fraction depends on the
temperature at which it evaporates.
Endothermic peak 2 in the temperature range 38 – 105°C
represents energy losses for vaporization of the free water
fraction with a maximum at 89.1°C. The experimental shape
of this peak in this temperature range is very typical of free
water [9]. DHQ contains mainly this type of water and,
Method for Quantitative Determination of Various Forms 579
5000
4500
4000
3500
3000
2500
2000
1500
0 2 4 6 8 10
2
1
Weight, mg
qi, J/g
Fig. 5. Specific heat of vaporization of fractions as a function of
weight change for group 2 samples: free water fraction (1) and
weakly bound water fraction (2).
TABLE 3. Physical Properties of Fractions Forming Peak A with
Variable Weight
Peak minit, mg
Parameter
Qi, mJ qi, J/g
{roman mole
roman {H sub
{2}
O}}over{roman
mole roman
DHQ}
1 1.03 24.592 839.9* 0.067**
1.97 33.671 0.058**
3.19 36.612 0.055**
3.91 55.675 0.042**
4.95 83.756 0.038**
6.14 85.602 0.036**
7.13 92.608 0.031**
8.41 115.342 0.03**
9.02 120.119 0.024**
10.05 126.156 0.021**
2 1.03 150.598 varies from
2400 to 2269
using Eq. 6
1.097
1.97 283.649 1.12
3.19 637.634 1.324
3.91 669.958 1.424
4.95 898.587 1.599
6.14 1264.654 1.411
7.13 1395.195 1.523
8.41 1405.256 1.543
9.02 1420.65 1.521
10.05 1596.63 1.54
3 1.03 58.339 2093.58 0.455
1.97 117.41 2798.062 0.545
3.19 303.943 3043.104 0.668
3.91 313.121 3072.723 0.717
4.95 438.756 3433.171 0.805
6.14 550.484 3636.445 0.868
7.13 718.453 3780.064 0.856
8.41 1070.953 4214.752 0.985
9.02 1900.943 4395.207 1.269
10.05 2292.181 4516.604 1.468
*
Handbook value.
**
Mole C
2
H
5
OH (peak 1 corresponds to evaporation of EtOH); i,
peak number.
therefore, it determines the total moisture of DHQ substance.
The quantitative content of the free water fraction is about
9.4%.
Endothermic peak 3 represents energy losses to evaporation
of the weakly bound water fraction with a maximum at
99°C in the temperature range 82 – 122°C. This type of water
is stable and difficultly removed by nondestructive drying.
However, it is less stable than strongly bound water, the
destruction of which occurs only with melting and destruction
of DHQ molecules. The quantitative content of the
weakly bound water fraction is about 2.7%.
Table 2 presents measurements of the physical characteristics
of the fractions forming peak A.
The measurements reflect well the behavior of the various
fractions of peak A if the weights of the group 1 samples
are similar enough.
Figure 4 shows the separation of the fractions forming
peak A for group 2 samples with variable weights. It can be
seen that the maximum temperatures of peaks 1 and 2 undergo
gradual and small shifts to higher temperatures as the
weight increases whereas such behavior is not observed for
peak 3. This is due to the fact that temperature gradients
throughout the sample in the container and thermal resistance
in the thermometer – container – sample chain do not
increase in proportion to the weight increase (and the distribution
of the sample within the container) [5, 10].
Table 3 presents measurements of the physical characteristics
of the fractions forming peak A with variable weight.
Figure 5 shows plots of the specific heats of vaporization
of the free and weakly bound water fractions as functions of
weight change. It can be seen that the specific heat of vaporization
of the free water fraction is practically constant as the
weight increases. The small trend can be explained by an increase
in the evaporation area as the weight increases.
A linear dependence is observed for the weakly bound
water fraction. The resulting specific heats of evaporization
are linearly related to the amount of substance. This dependence
can be explained by the presence in DHQ of binding
centers for water molecules. The substance first loses molecules
from the upper outer layer. The work for release of water
molecules from the inner layers is proportional to their
path within the substance because they interact with vacated
binding centers of higher lying layers, through which they
must pass. The path within the substance for these molecules
is proportional to the thickness of the substance layer inside
the container, i.e., the weight. The parameters of the linear
function can be used to estimate the bonding energy of water
molecules to DHQ. To a first approximation, extrapolation of
the line to zero weight can be used. This gives a value of
2125 J/g. The closest whole-number ratio for the number of
DHQ molecules used per molecule of weakly bound water
that corresponds to this estimate for the specific energy of
weakly bound water would be two DHQ molecules per molecule
of weakly bound water.
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th
Pushchino School-Conference of Young
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th
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th
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580 B. N. Boiko et al.
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