The novel low density MgxTiAlFeNiCr (x=0.6~2.0) high-entropy alloys were prepared by mechanical alloying, the relation of Mg content, thermodynamic parameter and phase structure was researched. The results showed that the prepared high-entropy alloy powders were approximately spherical particles with a diameter about 3 μm. The measurements of X-ray diffraction (XRD) and analyses of energy-dispersive X-ray spectrometry (EDS) revealed that Mg had a high solid solubility in BCC (body center cubic) lattice. The results of thermodynamic calculation showed that the alloys (x=0.6~1.4) had a single BCC1 phase when 8.68%≤δ≤9.77% (δ was atomic radii mismatches), 14.78 J/(mol?K)≤ΔSmix≤14.82 J/(mol?K) (ΔSmix was mixing entropy) and –14.13 kJ/mol≤ΔHmix≤–6.76 kJ/mol (ΔHmix was mixing enthalpy). However, the alloys (x=1.6~1.8) consisted of BCC1 and BCC2 phases when 10.0%≤δ≤10.1%, 14.65 J/(mol?K)≤ΔSmix≤14.74 J/(mol?K) and –5.40 kJ/mol≤ΔHmix≤–4.19 kJ/mol. When x≥2.0, Mg content exceeded the solid solubility of Mg in BCC1 and BCC2 lattices. As a result, Mg2.0TiAlFeNiCr alloy contained the main phases BCC1 and BCC2 and the minor phases Mg and intermetallic compound. The lattice constant (a) of BCC1 and BCC2 were determined respectively to be 0.289 and 0.291 nm by the XRD measurement and high resolution transmission electron microscope (HRTEM) analysis. For BCC1 phase, Fe acted as a solvent element whereas Mg, Ti, Al, Ni and Cr behaved like solute elements. For BCC2, however, Cr acted as a solvent element whereas Mg, Ti, Al, Fe and Ni behaved like solute elements. Compared with BCC1, high Mg content was achieved in BCC2 phase. Moreover, BCC1 and BCC2 displayed a semicoherent interface. The MgxTiAlFeNiCr (x=0.6~2.0) high-entropy alloys exhibited a good corrosion resistance in 3.5wt% NaCl solution. But the corrosion resistance decreased with the increasing of Mg in the alloys.
Tingzhi SI Qinghua LIU Wenxiang XU Xiaoli DING
. Phase evolution and corrosion resistance of MgxTiAlFeNiCr (x=0.6~2.0) high-entropy alloys[J]. The Chinese Journal of Process Engineering, 2019
, 19(2)
: 393
-399
.
DOI: 10.12034/j.issn.1009-606X.218204
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