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ORIGINAL ARTICLE
9 (
1_suppl
); S570-S575
doi:
10.1016/j.arabjc.2011.06.029

Structural effects and thermal decomposition kinetics of chalcones under non-isothermal conditions

Department of Chemistry, Annamalai University, Annamalainagar 608 002, India

⁎Corresponding author. Tel.: +91 4144 239523, mobile: +91 9488476098. pvta1998@yahoo.co.in (V. Thanikachalam)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

Two chalcones namely, 1,5-bis(4-hydroxy-3-methoxyphenyl)pentan-1,4-dien-3-one (BHMPD) and 2,5-bis(4-hydroxy-3-methoxybenzylidene)cyclopentanone (BHMBC) have been synthesised and characterized by microanalysis, FT-IR, mass spectra and NMR (1H and 13C) techniques. The thermal decomposition of these compounds was studied by TGA and DTA under dynamic nitrogen atmosphere at different heating rates of 10, 15 and 20 K min−1. The kinetic parameters were calculated using model-fitting (Coats–Redfern, CR) and model-free methods (Friedman, Kissinger–Akahira–Sunose, KAS and Flynn–Wall–Ozawa, FWO). The decomposition process of BHMPD and BHMBC followed a single step mechanism as evidenced from the data. Existence of compensation effect was noticed for the decomposition of these compounds. Invariant kinetic parameters are consistent with the average values obtained by Friedman and KAS isoconversional method in both compounds.

Keywords

Cyclopentanone
Dienone
Thermal decomposition
Kinetic parameters
Model-fitting
Model-free analysis
1

1 Introduction

Curcumins have several biological activities, such as anti-inflammatory, antioxidative, antibacterial, antihepatotoxic, hypertensive and hypocholesterolemic properties (Chang et al., 2003; Sharma, 1976; Sharma et al., 1972, Gafner et al., 2004; Bennett, 1986). Curcumin inhibits in vitro lipid peroxide formation by liver homogenates of endemic mice (Tonnesen, 1986). It is used for the synthesis of bioactive pyrimidine compounds (Das et al., 2006) and also finds applications in the preparation of liquid–crystalline polymers (Gangadhara and Kishore, 1995). Thermotropic liquid crystalline behavior of polymeric materials containing cyclopentanone moiety linked with polyethylene spacers is of considerable current interest, not only because of their potential as high-strength fibers, plastics, moldings, etc. (Griffin and Johnson, 1984; Blumstein, 1985; Chapoy, 1986), but also of their applications in non-linear optical materials (Kawamata et al., 1996). The benzylidene derivatives are intermediates in various pharmaceuticals, agrochemicals and perfumes (Ogawa et al., 1988). Curcumin demonstrated a great ability in chelating essential metal ions such as Cu(II) (John et al., 2002) and the complexes showed a higher scavenging ability than curcumin. The aim of this work is to determine the thermal stability and decomposition mechanism of chalcones.

In this paper, we report the synthesis of 1,5-bis(4-hydroxy-3-methoxyphenyl)pentan-1,4-dien-3-one (BHMPD) and 2,5-bis(4-hydroxy-3-methoxybenzylidene)cyclopentanone (BHMBC) and their thermal decomposition in non-isothermal dynamic nitrogen atmosphere condition. The kinetic and thermodynamic parameters are determined using model-fitting and model-free methods.

2

2 Experimental

2.1

2.1 Materials

All the chemicals were of AnalaR grade, purchased from Sd fine chemicals and were used as such without further purifications.

2.2

2.2 Instruments

Elemental analyzes were performed on a Carlo Analyzer at Central Drug Research Institute (CDRI), Lucknow, India. FT-IR spectra were recorded in a KBr-pellet on an Avatar-330 spectrometer (with resolution 2 cm−1). The mass spectra were recorded on a JEOL Gcmate, at the Indian Institute of Technology, Chennai, India. The NMR spectra were recorded on a Bruker AMX 400 MHz for 1H and 100 MHz for 13C NMR with TMS as an internal standard at the Indian Institute of Science, Bangalore, India. The simultaneous TGA and DTA curves were obtained with the thermal analysis system model Perkin Elmer TAC 7/DX Thermal Analysis Controller TAC-7. The TG and DTA analyzes of BHMPD and BHMBC were carried out under dynamic nitrogen atmosphere (100 mL min−1), in an alumina crucible with a sample mass around 10 mg with heating rates of 10, 15 and 20 K min−1 from 35 to 700 °C. The kinetic parameters Ea and ln A were calculated using Microsoft® Excel Software. The sample temperature, which is controlled by a thermocouple, did not exhibit any systematic deviation from the preset linear temperature program.

2.3

2.3 Synthesis of BHMPD

Dry HCl gas was passed through a solution containing vanillin (1 mmol) and acetone (0.5 mmol) in dry methanol. The solution turned dark pink and yellow precipitate was obtained after the addition of water. It was purified by crystallization from methanol medium (m.p. = 99 °C; lit. = 98–99 °C) (Du et al., 2006).

Elemental analysis: Calculated = C, 70.13; H, 5.19. Found = C, 70.48; H, 5.17. FT-IR (KBr disk, cm−1): ν C O = 1667 , ν C C = 1591 , 1511 , ν C H = 1428 and ν OH = 3177 . 1H NMR (CDCl3, δ ppm): 3.82 (methoxy proton), 6.94–7.38 (aromatic protons), 7.40, 9.73 (vinyl protons of the α,β-unsaturated arylidene system), 10.26 (phenolic —OH). 13C NMR (CDCl3, δ ppm): 55.46 (methoxy carbon), 110–148 (aromatic carbons and vinyl carbons), 152.97 (C—O carbons of the α,β-unsaturated arylidene system, 190.86 (carbonyl carbon of arylidene keto moiety).

2.4

2.4 Synthesis of BHMBC

Vanillin (1 mmol) and cyclopentanone (0.5 mmol) were heated in a water bath (45–50 °C) until a clear solution was obtained, concentrated hydrochloric acid was then added followed by 2 h stirring. After standing overnight, the mixture was treated with cold aqueous acetic acid (1:1) and filtered. The solid material was washed first with cold ethanol, then with hot water and dried in vacuum. The yellow substance was recrystallized from ethanol (m.p. = 212 °C; lit. = 212–214 °C) (Du et al., 2006).

Elemental analysis: Calculated = C, 71.59; H, 6.68. Found: C, 71.23; H, 6.57. FT-IR (KBr disk, cm−1): ν C O = 1667 , ν C C = 1617 , ν C H = 3005 , ν C C = 1519 and ν C H = 1421 . 1H NMR (CDCl3 and DMSO-d6, δ ppm): 7.31 (2H, —OH protons), 6.97–6.98 (2H, aromatic hydrogen), 7.52 (2H, —CH⚌), 3.94 (6H, OCH3 protons), 2.15–2.17 (4H, —H2C—CH2—). 13C NMR (CDCl3, δ ppm): 195.89 (C⚌O), 148.06–147.32 (CH, C⚌C, C—O), 113–134.66 (aromatic carbons), 55.77 (OCH3), 26.32 (CH2).

3

3 Theoretical background

3.1

3.1 Model fitting method

The integral method of Coats and Redfern has been most successfully used for studying the kinetics of dehydration and decomposition of different solid substances (Horowitz and Metzger, 1963; Coats and Redfern, 1964; Wendlandt, 1974; Sestak, 1984). The kinetic parameters can be derived from modified Coats and Redfern equation:

(1)
ln g ( α ) T 2 = ln AR β E a 1 - 2 RT E a ln AR β E a - E a RT , where g(α) is an integral form of the conversion function, the expression of which depends on the kinetic model of the occurring reaction. If the correct g(α) function is used, a plot of ln [g(α)/T2] against l/T should give a straight line from which the values of the activation energy, Ea and the pre-exponential factor, A can be calculated.

3.2

3.2 Model free methods

Friedman method (Friedman, 1963) is a different method and was one of the first isoconversion methods. The logarithm of the non-isothermal rate law:

(2)
β d α dT = Ae - E a RT f ( α ) , gives
(3)
ln β d α dT = ln A α f ( α ) - E a , α RT α .
Flynn–Wall–Ozawa equation (Flynn and Wall, 1966; Ozawa, 1965):
(4)
ln β = ln 0.0048 AE a g ( α ) R - 1.0516 E a RT ,
and Kissinger–Akahira–Sunose (KAS) equation (Kissinger, 1957; Akahira and Sunose, 1971):
(5)
ln β T 2 = ln AE a g ( α ) R - E a RT .

The plots of ln (βdα/dT) Vs 1/T (Eq. (3)), ln β Vs 1/T (Eq. (4)) and ln (β/T2) Vs 1/T (Eq. (5)) have been shown to give the values of apparent activation energies for the decomposition of BHMPD and BHMBC at different values of α. According to these equations, the reaction mechanism and shape of g(α) function do not affect the values of the activation energies of the decomposition stage.

3.3

3.3 Invariant kinetic parameters (IKP) method

The invariant kinetic parameters were obtained by the method of Lesnikovich and Levchik (1983). The straight lines obtained for the plots of ln Aβ Vs Eβ for several constant heating rates should intersect at a point (Lesnikovich and Levchik, 1985) which corresponds to the true values of activation energy and pre-exponential factor, which are called invariant kinetic parameters (Einv, Ainv). The evaluation of the invariant kinetic parameters is performed using the supper correlation equation:

(6)
α β = ln A inv - b β E inv .

The plot of aβ Vs bβ, obtained for three constant heating rates, is a straight line (Flynn, 1997) whose parameters allow the determination of ln Ainv and Einv.

3.4

3.4 Thermodynamic parameters

The kinetic parameters, energy of activation and pre-exponential factor obtained from Kissinger single point (Kissinger, 1957, 1956; Patel and Chaudhri, 1978; Whelan et al., 1984) kinetic method uses the Eq. (7):

(7)
ln ( β / T m 2 ) = - E a / RT m + ln ( AR / E a ) , where, Tm is temperature that corresponds to the maximum of /dT. This ‘model-free’ kinetic method can be applied with a reasonable approximation without being limited to n-order kinetics (Malek, 1989), providing a single Ea value for each reaction step. For this reason, it is often defined as a Kissinger single point method. If the reaction proceeds under conditions where thermal equilibrium is always maintained, then a plot ln ( β / T m 2 ) Vs 1/Tm gives a straight line with a slope equal to −Ea/R.

Based on the values of activation energy and pre-exponential factor for the decomposition stage, the values of Δ S , Δ H , Δ G for the formation of activated complex from the reactant were calculated according (Malek, 1989; Bamford and Tipper, 1980; Cordes, 1968) to, equations:

(8)
Δ S = R ln Ah e χ kBT p . Since
(9)
Δ H = E a - RT p ,
(10)
Δ G = Δ H - T p Δ S .

4

4 Results and discussion

4.1

4.1 Non-isothermal TG and DTA

The TG and DTA thermograms of pure BHMPD and BHMBC were recorded in a dynamic nitrogen atmosphere at different heating rates of 10, 15 and 20 K min−1 and presented in Figs. S1 and S2 and show those two distinct endothermic peaks on account of melting and decomposition. The thermal decomposition process of BHMPD and BHMBC in one stage was observed from the TG curves. The decomposition processes of BHMPD and BHMBC are completed 99.2% and 67% with endothermic peaks, respectively. The decomposition process of BHMPD starts from 180 °C and ends at 280 °C whereas that for BHMBC starts from 300 °C and ends at 480 °C.

4.2

4.2 Non-isothermal decomposition reaction kinetics

The heating rates 10, 15 and 20 K min−1 were selected to study the decomposition process of chalcones. The values of α ranging from 0.22 to 0.80 for BHMPD and 0.20 to 0.70 for BHMBC with an increment of 0.02 were chosen for kinetic calculations.

The values of energy of activation corresponding to the values of α for the decomposition procedure obtained by Friedman (Friedman, 1963), Kissinger–Akahira–Sunose (Kissinger, 1957; Akahira and Sunose, 1971) and Flynn–Wall–Ozawa (Flynn and Wall, 1966; Ozawa, 1965) are shown in Fig. 1. It is clear that the value of Ea increases with α values and remains constant from 0.20 to 0.80 for BHMPD and 0.2 to 0.70 for BHMBC the increases with increasing α indicating removal of gaseous products from solid mass. Therefore, the decomposition stage could be recorded as a single step process (Vyazovkin and Wight, 1997). The apparent activation energy varied with increasing conversions and the average value is 100.71 ± 0.14 kJ mol−1 for BHMPD and 128.99 ± 0.25 kJ mol−1 for BHMBC (Friedman method). The meager dependence of activation energy on the extent of conversion suggests that the decomposition took place in a single step for BHMPD and BHMBC. BHMBC compound has higher energy of activation than BHMPD, which indicates cyclic compound thermally more stable than acyclic compound. The mass spectral data of these compounds show that compounds are decomposed instead of sublimation.

Ea versus α plot for the decomposition of BHMPD and BHMBC under non-isothermal condition.
Figure 1
Ea versus α plot for the decomposition of BHMPD and BHMBC under non-isothermal condition.

4.3

4.3 Invariant kinetic parameters (IKP) analysis

The invariant kinetic parameter method was applied to the data calculated for the heating rates of 10, 15 and 20 K min−1. The evaluation of the kinetic parameters was performed using Coats–Redfern method. For these kinetic models in the range 0.2 ⩽ α ⩽ 0.8 for BHMPD and 0.2 ⩽ α ⩽ 0.7 for BHMBC, the straight lines corresponding to Coats–Redfern method is characterized by correlation coefficient values close to unity. The values of Ea and ln A depend on the kinetic model as well as on the heating rate, as shown in Tables 1 and 2.

Table 1 Apparent kinetic parameters by Coats–Redfern equation for each applied heating rate for BHMPD.
Kinetic model β = 10 K min−1 β = 15 K min−1 β = 20 K min−1
Ea/kJ mol−1 ln A A/s−1 r Ea/kJ mol−1 ln A A/s−1 r Ea/kJ mol−1 ln A A/s−1 r
P2 26.63 3.62 0.999 26.31 3.83 0.999 26.37 4.01 0.999
P3 14.86 0.45 0.999 14.61 0.71 0.999 14.61 0.91 0.999
P4 9.01 −1.33 0.999 8.80 −1.05 0.999 8.76 −0.84 0.999
F1 89.88 19.42 0.996 88.36 19.14 0.993 88.22 19.04 0.991
F2 126.30 28.59 0.985 123.27 27.84 0.980 122.55 27.47 0.978
F3 170.40 39.55 0.972 165.40 38.19 0.967 163.92 37.50 0.963
D1 143.26 38.51 0.999 142.37 38.24 0.999 143.14 38.17 0.963
D2 148.42 31.84 0.999 146.96 31.40 0.998 147.40 31.21 0.999
D3 167.92 35.19 0.998 165.76 34.52 0.996 165.92 34.19 0.995
D4 164.42 34.13 0.999 162.87 33.61 0.998 163.54 33.41 0.997
A2 40.64 7.46 0.995 39.82 7.50 0.992 39.69 7.59 0.989
A3 23.92 3.14 0.994 23.35 3.29 0.990 23.21 3.43 0.987
A4 16.01 0.95 0.992 15.55 1.14 0.987 15.42 1.30 0.983
R2 74.84 14.89 0.999 73.87 14.79 0.997 73.95 14.79 0.996
R3 70.86 14.04 0.999 69.65 13.99 0.998 69.79 14.02 0.998
Table 2 Apparent kinetic parameters by Coats–Redfern equation for each applied heating rate for BHMBC.
Kinetic model β = 10 K min−1 β = 15 K min−1 β = 20 K min−1
Ea/kJ mol−1 ln A A/s−1 r Ea/kJ mol−1 ln A A/s−1 r Ea/kJ mol−1 ln A A/s−1 r
P2 50.36 6.83 0.995 47.08 6.35 0.992 49.86 7.08 0.991
P3 29.97 2.72 0.994 27.69 2.48 0.990 29.39 3.08 0.989
P4 19.84 0.52 0.992 18.05 0.39 0.987 19.31 0.94 0.985
F1 133.50 22.87 0.999 133.74 22.82 0.999 140.76 24.23 0.999
F2 158.69 27.95 0.999 168.23 29.59 0.999 177.41 31.35 0.999
F3 186.90 33.59 0.999 208.33 37.40 0.995 220.09 39.57 0.996
D1 248.62 51.27 0.997 236.40 48.47 0.995 247.40 50.47 0.994
D2 247.21 42.67 0.997 238.48 40.51 0.996 250.16 42.62 0.996
D3 262.38 44.16 0.998 258.27 42.83 0.998 271.14 45.13 0.998
D4 289.86 49.12 0.995 275.59 45.76 0.994 288.33 48.02 0.993
A2 61.41 9.18 0.999 61.38 9.33 0.999 64.84 10.20 0.999
A3 36.91 4.29 0.999 36.79 4.50 0.998 39.05 5.19 0.998
A4 25.36 1.85 0.998 25.20 2.09 0.997 26.88 2.70 0.998
R2 122.0 19.86 0.998 118.72 19.15 0.996 124.81 20.41 0.997
R3 118.57 19.42 0.997 114.22 18.53 0.997 120.04 19.75 0.995

For several groups of apparent activation parameters, obtained by different kinetic models, we tried to establish the best combination (r → 1), a better resolution in determining the invariant kinetic parameters and the closest value to the mean isoconversional activation energies (Budrugeac and Segal, 2007; Vyazovkin and Lesnikovich, 1988; Pratap et al., 2007). For (all kinetics models) AKM–{F2; F3; D1; D2; D3; D4}, the plot of ln A Vs Ea has the highest correlation coefficient (r = 0.988) and is a true straight line for BHMPD whereas for AKM–{F2; F3; D1; D2; D3; D4; R2; R3}, the plot of ln A Vs Ea has the highest correlation coefficient (r = 0.999) and is a true straight line for BHMBC. Depending on the choice of kinetic models, the compensation effect parameters are obtained with different accuracies, their values and derived invariant activation parameters varying substantially.

For AKM–{F2; F3; D1; D2; D3; D4}, the invariant kinetic parameters are Einv = 91.02 kJ mol−1 and ln Ainv = 19.41 (Table S1) obtained with r = 0.988 for BHMPD and AKM–{F2; F3; D1; D2; D3; D4; R2; R3}, the invariant kinetic parameters are Einv = 128.75 kJ mol−1 and ln Ainv = 22.05 (Table S2) obtained with r = 0.999 for BHMBC, respectively. For these groups, the invariant activation energy is slightly above 103.06 kJ mol−1, close to 99.06 ± 0.28 kJ mol−1, 97.69 ± 0.14 kJ mol−1 obtained by Friedman and KAS method for BHMPD and for BHMBC is slightly above 128.77 kJ mol−1, close to 126.80 ± 0.24 kJ mol−1 obtained by KAS method (Tables S1 and S2). The higher Ea value for BHMBC may be due to the ring system that influences the stability of the compound and also BHMBC is thermally more stable, because of decomposition that starts at >320 °C at all heating rates (Fig. S2).

The most probable kinetic model for decomposition process of BHMPD and BHMBC is R2 and F1 models, respectively. By introducing the derived reaction model for BHMPD, g(α) = [1 − (1 − α)1/2], the following Eq. (11) is obtained:

(11)
1 - ( 1 - α ) 1 / 2 = AE a R β p ( x ) .

The plot of [1 − (1 − α)1/2] against (Ea p(x)/) at the different heating rates is constructed in Fig. S3, and for BHMBC is, g(α) = −ln (1 − α), the following Eq. (12) is obtained:

(12)
- ln ( 1 - α ) = AE a R β p ( x ) .

The plot of −ln (1 − α) against (Ea/) p(x) at different heating rates is constructed and is similar to Fig. S3.

By using the above equations, the A value was determined from the slope of the fitted line shown in Fig. S3. For contracting area model (R2) and Ea = 99.06 ± 0.28 kJ mol−1, the pre-exponential (frequency) factor was found to be A = 8.92 × 108 min−1 (ln A = 20.60) for BHMPD and for power law (F1) and Ea = 128.99 ± 0.25 kJ mol−1, the pre-exponential (frequency) factor was found to be A = 3.94 × 109 min−1 (ln A = 22.09) for BHMBC, respectively. The obtained value of ln A is in good agreement with average value of Friedman isoconversional intercept ln [A f(α)] = 20.92 for BHMPD and 21.47 for BHMBC, respectively.

4.4

4.4 Thermodynamic parameters

From the DTA curves, the peak temperatures for BHMPD are 542.6, 548.3 and 557.6 K and for BHMBC are 676.58, 686.31 and 696.21 K. These peak temperatures are used to evaluate single point kinetic parameters. The obtained values are 103.71 and 124.32 kJ mol−1 for BHMPD and BHMBC, respectively. The obtained values are in good agreement with values obtained by Friedman method for both compounds.

The thermodynamic parameters, Δ S , Δ H and Δ G were calculated at the peak temperature Tm in the DTA curves for the corresponding stage, since the temperature characterizes the higher rate of decomposition and therefore, it is an important parameter.

As can be seen from the Table 3, the value of Δ S for the decomposition stage is negative for both the compounds. It means that the corresponding activated complexes were with high degree of arrangement than the initial state. The positive values of Δ H and Δ G for both the compounds show that they are connected with absorption of heat and they are non-spontaneous processes (Criado et al., 2005; Sokolskii and Druz, 1981). The obtained Ea values are coincided with invariant parameters. Energy of activation of BHMBC has a higher value than that of BHMPD which indicates that BHMBC is thermally more stable than BHMPD.

Table 3 Values of kinetic and thermodynamic parameters for the thermal decomposition of BHMPD and BHMBC in nitrogen atmosphere.
Parameter BHMPD BHMBC
Ea/kJ mol−1 103.71 124.32
ln A A/s−1 22.14 20.98
ΔS/J K−1 mol−1 −64.84 −74.45
ΔH/kJ mol−1 99.71 120.32
ΔG/kJ mol−1 130.88 156.12
r −0.969 −0.995

5

5 Conclusions

The studied compounds decomposed in a single stage with the absorption of heat. The model for the decomposition mechanism is R2 for BHMPD and F1 for BHMBC, respectively. The thermal stability of BHMPD is less than that of BHMBC. Since the energy of activation for the former is lesser than the cyclopentanone derivative, which indicates that the ring structure influenced the thermal stability of the compound. Mass spectra show that these compounds are decomposed instead of sublimation.

Acknowledgments

The authors thank Dr. N. Jayachandramani, Professor and Head, Department of Chemistry, Pachaiappa’s College, Chennai for his fruitful suggestions and The Head, Indian Institute of Technology, RISC, Chennai for TGA–DTA measurements.

References

  1. , , . Inst. Technol.. 1971;16:22.
  2. , , . Comprehensive chemical kinetics. Reactions in the Solid State. Vol Vol. 22. Amsterdam: Elsevier; .
  3. , . Prog. Lipid Res.. 1986;25:539.
  4. , . Polymeric Liquid Crystals. New York: Plenum Press; .
  5. , , . J. Therm. Anal. Calorim.. 2007;88:703.
  6. , , , , , , , , . Biochem. Pharmacol.. 2003;65:2009.
  7. , . Recent Advances in Liquid Crystalline Polymers. London: Elsevier; .
  8. , , . Nature (London). 1964;201:68.
  9. , . J. Phys. Chem.. 1968;72:2185.
  10. , , , . J. Therm. Anal. Calorim.. 2005;82:671.
  11. , , , , . J. Mol. Catal. A. 2006;247:182.
  12. , , , , , , , , . Eur. J. Med. Chem.. 2006;41:213.
  13. , . Thermochim. Acta. 1997;300:83.
  14. , , . J. Res. Nat. Bur. Stand. A. 1966;70:487.
  15. , . J. Polym. Sci. C. 1963;6:183.
  16. , , , , , , , , , . Phytochemistry. 2004;65:2849.
  17. , , . Polymer. 1995;36:1903.
  18. , , . Liquid Crystals and Ordered Fluids. New York: Plenum Press; .
  19. , , . Anal. Chem.. 1963;35:1464.
  20. , , , . J. Exp. Clin. Cancer Res.. 2002;21:219.
  21. , , , , , , . Chem. Phys. Lett.. 1996;249:29.
  22. , . J. Res. Natl. Bur. Stand.. 1956;57:217.
  23. , . Anal. Chem.. 1957;29:1702.
  24. , , . J. Therm. Anal.. 1983;27:89.
  25. , , . J. Therm. Anal.. 1985;30:237.
  26. , . Thermochim. Acta. 1989;138:337.
  27. Ogawa, M., Ishiim, Y., Nakno, T., Irifune, S., 1988. Jpn. Kohai Tokyo JP 63192446, A2 (Chem. Abstr. 63, 238034).
  28. , . Bull. Chem. Soc. Jpn.. 1965;38:1881.
  29. , , . Thermochim. Acta. 1978;25:247.
  30. , , , , . J. Therm. Anal. Calorim.. 2007;89:399.
  31. , . Thermodynamical Properties of Solids. Prague: Academic; .
  32. , . Biochem. Pharmacol.. 1976;25:1811.
  33. , , , , . Biochem. Pharmacol.. 1972;21:1210.
  34. , , . Introduction in Theory Heterogeneous Catalysis. Moscow: Vyshaya Shkola; . (in Russian)
  35. Tonnesen, H.H., 1986. Ph.D. Thesis. Institute of Pharmacy, University of Oslo, Norway.
  36. , , . Thermochim. Acta. 1988;128:297.
  37. , , . Annu. Rev. Phys. Chem.. 1997;48:125.
  38. , . Thermal Methods of Analysis. New York: John Wiley and Sons Inc.; .
  39. , , , . Thermochim. Acta. 1984;80:149.

Appendix A

Supplementary material

Supplementary data associated with this article can be found, in the online version, at doi:10.1016/j.arabjc.2011.06.029.

Appendix A

Supplementary material

Supplementary data 1

Supplementary data 1 Supplementary tables and figures

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