Melting and solidi cation of Pb nanoparticles embedded in an Al matrix as studied by temperature-modulated di erential scanning calorimetry

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PHILOSOPHICAL MAGAZINE LETTERS, 1998, VOL. 78, NO. 1, 37± 44 Melting and solidi cation of Pb nanoparticles embedded in an Al matrix as studied by temperature-modulated di erential scanning calorimetry By Y. Li, S. C. Ng, Z. P. Lu Department of Materials Science, Science Faculty, National University of Singapore, Singapore 119260 Y. P. Feng Department of Physics, Science Faculty, National University of Singapore, Singapore 119260. and K. Lu State Key Laboratory of Rapidly Solidi ed Non-equilibrium Alloys, Institute of Metal Research, Chinese Academy of Sciences, Shenyang 110015, PR China [Received 23 December 1997 and accepted 12 March 1998] Abstract A newly developed temperature-modulated di erential scanning calorimetry has been used to study the melting and solidi cation processes of Pb nanoparticles embedded in an Al matrix under continuous heating and cooling conditions at rates of 1± 5Kmin - 1. Endothermic peaks have been observed in the total, the reversing and the non-reversing heat ows during the melting process, indicating that the process is controlled by both thermodynamics and kinetics. As the underlying heating rate increases, the enthalpy change in the reversing heat ow increases whereas that in the non-reversing heat ow decreases, while that in the total heat ow remains constant. On the other hand, during solidi cation, exothermic peaks are observed only in the non-reversing and total heat ow curves and the enthalpy changes remain essentially constant when the underlying cooling rates increase from 1 to 5Kmin - 1. No exothermic peaks were observed in the reversing heat ow curve. This indicates that the solidi cation process is controlled essentially by kinetics. 1. Introduction Di erential scanning calorimetry (DSC) is a widely used method to measure heats and temperatures for various phase transitions which involve thermal e ects. In DSC measurements, the sample temperature is either ramped linearly at a constant heating (or cooling) rate or kept constant as in isothermal experiments. The measured heat ow can be described by the following equation: dh dt = - c p b + f (T,t), (1) where H is the amount of heat evolved, c p the heat capacity, b the heating rate, T the absolute temperature and t the time. It states that the heat ow measured in a DSC cell, which is referred to as total heat ow (HF), is made up of two terms. The rst term is a function of the heat capacity of the sample and the heating rate, which is 0950± 0839/98 $12.00 Ñ 1998 Taylor & Francis Ltd.

38 Y. Li et al. denoted as the thermodynamic or reversing heat ow (RHF). The second term is a function of absolute temperature and time, which governs the kinetics and is denoted as the non-reversing heat ow (NHF). The measured heat ow in DSC is the total heat ow including both the RHF and the NHF. Recently, an enhanced version of the DSC method, temperature± modulated di erential scanning calorimetry (MDSC) has been introduced (Reading 1993, Reading et al. 1993). The bene ts of the MDSC method have been documented in several recent publications (O Reilly and Cantor 1996, Ishikiriyama et al. 1997, Ishikiriyama and Wunderlich 1997). One of advantages of the MDSC is that it is able to separate the RHF and the NHF from the HF during a phase transition. In MDSC, the sample temperature is modulated sinusoidally about a constant ramp so that the temperature at time t is T = T 0 + b t + A sin ( 2p t p ), where T 0 is the initial temperature, A the amplitude of the modulation and p the period. The resulting instantaneous heating rate dt/dt varies sinusoidally about the average underlying heating rate b. The apparatus measures the amplitude of the instantaneous heat ow and the average heat ow (which is the HF). By carrying out a suitable Fourier deconvolution of the measured quantities, both the RHF and the NHF can be determined. It is noted that no such information could be determined hitherto with the conventional DSC method. The melting of crystalline solids is an important phase transition in materials science. The special capability of MDSC to separate the RHF and the NHF from the signals makes it useful to study the rst-order phase transitions such as melting and solidi cation (O Reilly et al. 1996). MDSC has been used to investigate melting and crystallization processes in several polymers and in pure In under quasi-isothermal condition (Ishikiriyama et al. 1997, Ishikiriyama and Wunderlich 1997). However, no experimental results have been reported to date on melting and solidi cation in metals using MDSC under the condition of continuous heating. This is probably because melting of metals normally takes place within a very narrow temperature range (a few kelvins) during heating, a range within which it is di cult to collect accurately four modulated cycles for a Fourier deconvolution. The collection of at least four modulated cycles within a transition is a basic requirement for MDSC to work properly. Recently it was reported that the melting of the Pb nanoparticles embedded in an Al matrix took place over a temperature range of about 30K as determined by a conventional DSC (Sheng et al. 1996). This made it possible to study the melting behaviour of pure metals by MDSC, since for such a large temperature range the four modulation cycles are easily collected. In this work, we present the rst MDSC study on the melting and freezing of metals under continuous heating and cooling conditions with the aim of revealing new information about these transformation processes. 2. Experimental details Commercial elemental powder blends of Al and Pb (purity, 99.999%; particle size, less than 100 mesh) with a composition of Al± 10 wt%pb were used as starting materials for ball milling. Ball milling was performed in a vibratory ball mill protected by an Ar atmosphere. High-hardness chrome steel balls of good wear resistance were used; the ball-to-powder weight ratio was 30 to 1 and the milling time was

Pb nanoparticles in Al matrix 39 10h. The as-milled Pb± Al samples were examined by X-ray di raction (XRD) and transmission electron microscopy (TEM). Both XRD and TEM experiments indicated that the as-milled product was a nanostructured mixture of pure Al and Pb phases and no alloying e ect between Al and Pb was observed. The mean particle size of Pb estimated from XRD and TEM measurements was about 15nm. The shape of the Pb nanoparticles embedded in the Al matrix was irregular and no epitaxial orientational relationship between Pb and Al could be identi ed from TEM observations. This means that random incoherent interfaces were formed between Pb and Al in the as-milled samples. The MDSC experiments were carried out on a temperature-modulated di erential scanning calorimeter (TA Instruments Inc. USA) using a refrigerated cooling system and a N 2 -gas DSC cell purge. The modulated DSC regime was used to measure the modulated heat ow in both heating and cooling up to 400 ë C. In order to obtain accurate and reproducible results, three experimental parameters need to be controlled in MDSC measurements, namely the underlying heating rate, the oscillation amplitude and the oscillation period. The underlying heating and cooling rates were from 1 to 5Kmin - 1, with the oscillation amplitude between 0.1 and 0.2K and the modulation period from 40 to 60s. The oscillation amplitudes and periods were determined so that at least four modulation runs could be performed during melting and freezing of Pb nanoparticles and the modulated heating and cooling rates were above 0Kmin - 1. Figure 1 illustrates the modulated heating ow and modulated heating rate for a MDSC run at a underlying heating rate of 2Kmin - 1, showing good control of conditions. The MDSC runs were repeated for the same sample of about 40 mg at least three times, and measurements of temperature and enthalpy changes were made on the third run. Figure 1. Modulated heating rate and modulated heat ow as functions of temperature under a underlying heating rate of 2Kmin - 1 showing well controlled conditions in the MDSC run.

40 Y. Li et al. 3. Results and discussion Figure 2(a) shows MDSC results obtained at an underlying heating rate of 2Kmin - 1 with an oscillation amplitude of 0.2K and a period of 60s. Evidently there is an endothermic peak in the HF corresponding to the melting process of Pb nanoparticles. The onset temperature is determined to be 317.4 ë C, which is about 10 ë C below the equilibrium melting point for Pb bulk crystal (327.2 ë C). The meltingpoint depression for the Pb nanoparticles embedded in an Al matrix was discussed by Sheng et al. (1996) and was attributed to the increase incoherent Pb± Al interfaces which acted as heterogeneous nucleation sites for the melting of Pb. A summary of characteristic temperatures obtained by MDSC under various underlying heating and cooling rates is given in Table 1. The integrated peak area, that is the total enthalpy change during melting of Pb nanoparticles, is about 10.1Jg - 1 (Pb), which is also smaller than the fusion enthalpy change for bulk Pb (24.0Jg - 1 ) (Smithells and Brandes 1976). Such a depression arises from the increase in Pb± Al interfaces, as addressed by Sheng et al. (1996). Endothermic peaks were detected corresponding to the melting process in the RHF and NHF curves respectively, which have similar shapes and characteristic (onset and peak) temperatures as those in the HF curve. The enthalpy changes for the RHF and NHF peaks are 5.7J g - 1 and 4.0J g - 1 (a) Figure 2. (a) HF, RHF and NHF functions of temperature under a underlying heating rate of 2Kmin - 1 showing endothermic reaction during melting of a Pb nanoparticle embedded in an Al matrix.

Pb nanoparticles in Al matrix 41 (b) Figure 2. (b) HF, RHF and NHF as functions of temperature under a underlying cooling rate of 2Kmin - 1 showing exothermic peaks for only the HF and the NHF. respectively. The sum of these two enthalpy changes (9.7J g - 1 ) is close to the HF (10.1J g - 1 ). The enthalpy change in the RHF is a measure of energy absorbed by the sample to raise its heat capacity, that is the thermodynamic enthalpy change. The enthalpy change in the NHF, however, is the energy absorbed by the sample to drive the melting process kinetically. The above results clearly indicate that the melting process of Pb nanoparticles embedded in an Al matrix under an underlying heating rate of 2Kmin - 1 is controlled by both thermodynamic and kinetic processes. Figure 2(b) shows the MDSC results obtained at an underlying cooling rate of 2Kmin - 1 with an oscillation amplitude of 0.2K and a period of 60s. An exothermal peak is seen in the HF curve, indicating a solidi cation process of the liquid Pb nanoparticles. A similar exothermal peak is detected in the NHF curve, but no exothermal peak is seen in the RHF curve, apart from a tiny bump. The integrated peak area for the HF peak is roughly equal to that for the NHF peak for the freezing of Pb. This result indicates that the freezing process of Pb nanoparticles embedded in an Al matrix under a cooling rate of 2Kmin - 1 is mainly kinetically controlled. Repeated heating and cooling MDSC measurements yield consistent results for melting and freezing in the Pb± Al nanogranular sample. Table 2 lists the enthalpy changes in the HF, the NHF and the RHF curves as functions of heating or cooling rate from 1 to 5Kmin - 1 respectively. It is seen that, with increasing heating rate, the RHF enthalpy change increases and the NHF enthalpy change decreases, while that of the HF remains constant ( gure 3). An increase in the underlying heating rate results in a decrease in the energy fraction for the kinetic process of melting. At an underlying heating rate of 5Kmin - 1, the NHF

42 Y. Li et al. Table 1. Characteristic temperatures of melting and solidification processes. Melting ë ë Heating or T onset ( C) T p ( C) cooling rate (K min - 1 ) HF RHF NHF HF RHF NHF Ð Ð 1 317.8 317.0 318.3 323.6 323.6 323.6 2 317.44 317.0 316.2 323.6 323.7 323.2 3 316.3 315.9 317.5 323.1 323.3 323.0 4 314.9 314.9 313.5 323.3 323.3 323.3 5 311.6 311.0 321.6 321.4 Solidification Heating or T onset1 ( ë C) T onset2 ( ë C) T p ( ë C) cooling rate (K min - 1 ) HF NHF HF NHF HF NHF 1 323.3 323.9 304.0 304.6 302.1 302.0 2 323.2 326.4 304.0 303.9 301.6 301.7 3 324.8 323.3 304.2 304.0 301.3 301.3 4 322.3 323.3 304.7 305.0 301.0 300.7 curve is essentially at and no endothermic peak can be detected, while the RHF enthalpy change increases to a value equivalent to that in the HF. This implies that the energy absorbed by the sample at a underlying heating rate of 5Kmin - 1 is totally used to raise the heat capacity. No energy is used to drive the kinetic process of melting due to the fast heating rate. On the other hand, in the solidi cation process, there is no cooling rate dependence of enthalpy change in the NHF and the HF, both being 14.5Jg - 1 at the cooling rates studied. This clearly con rms that the solidi cation process is essentially a kinetically controlled process. Finally, gure 4 shows the volume fraction melted as a function of temperature for the HF, the NHF and the RHF curves for a sample heated at a underlying heating rate of 2Kmin - 1. In conventional DSC measurements, the melting kinetics of a solid are normally analysed by means of the HF signals, which basically consists of both the kinetic and the thermodynamic contributions. By separating the HF into the RHF and the NHF in the MDSC measurement, one can evaluate the melting kinetics more accurately in terms of the NHF signals, which speci cally represent Table 2. Heat changes during melting and solidi cation of Pb nanoparticles embedded in an Al matrix measured by MDSC. Heat change (Jg - 1 ) Underlying heating Melting Solidi cation rate (Kmin - 1 ) HF RHF NHF HF RHF NHF 1 11.2 6 0.3 6.8 6 0.1 5.0 6 0.2 14.6 6 0.5 13.6 6 0.6 < 0 2 10.2 6 0.2 5.7 6 0.2 4.0 6 0.2 15.3 6 0.6 14.6 6 0.2 < 0 3 9.9 6 0.2 6.8 6 0.1 3.5 6 0.1 14.5 6 0.3 13.1 6 0.2 < 0 4 10.5 6 0.2 7.3 6 0.3 3.2 6 0.2 14.6 6 0.2 13.6 6 0.6 < 0 5 10.0 6 0.2 10.4 6 0.2 < 0 Ð Ð Ð

Pb nanoparticles in Al matrix 43 Figure 3. The enthalpy changes as a function of underlying heating rate for the HF, the RHF and the NHF. information on transformation kinetics. By integrating the partial area of each endothermic peak in the three heat ow curves, one can obtain the volume fraction melted as a function of temperature (assuming that the enthalpy change is proportional to the volume of liquid from melting). It is seen that these three curves are very similar in shape. A very small temperature lag can be observed between the HF and the kinetic (NHF) signals, especially at the beginning of the melting. When the melted volume fraction exceeds 50%, the three curves merge together. The present result shows that the di erence between the melting kinetics derived from the HF and those from the kinetic heat ow (NHF) is very small. This agrees with the previous observation in a melting study of Cd particles embedded in an Al matrix using conventional DSC as reported by Zhang et al. (1996). However, the measurements carried out in the present study are directly obtained from the thermodynamic and kinetic processes and are probably more accurate. 4. Conclusions A newly developed MDSC has been used to study the melting and solidi cation processes of Pb nanoparticles embedded in an Al matrix under continuous heating and cooling conditions at rates of 1± 5Kmin - 1. The results indicate that melting is controlled by both thermodynamic and kinetics, whereas solidi cation is controlled essentially by kinetics alone.

44 Pb nanoparticles in Al matrix Figure 4. Volume fraction of melt as a function of temperature for the HF, the RHF and the NHF under an underlying heating rate of 2Kmin - 1. REFERENCES Ishikiriyama, K., Boller, A., and Wunderlich, B., 1997, J. therm. Anal., 50(4), 547. Ishikiriyama, K., and Wunderlich, B., 1997, Macromolecules, 30, 4126. O Reilly, K. A. Q., and Cantor, B., 1996, Proc. R. Soc. A, 452, 2141. Reading, M., 1993, Trends Polym., 1, 248. Reading, M., Elliott, D., and Hill, V. L., 1993, J. therm. Anal., 40, 949. Sheng, H. W., Ren, G., Peng, L. M., Hu, Z. Q., and Lu, K., 1996, Phil. Mag. Lett., 73, 179. Smithells, C. J., and Brandes, E. A., 1976, Metals Reference Book, fth edition (London: Butterworth), p. 187. Zhang, D. L., Hutchinson, J. L., and Cantor, B., 1996, J. Mater. Sci., 29, 2147.