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K. Yasuda et al. / Journal of Physics and Chemistry of Solids 66 (2005) 443–447
and the reduction proceeds continuously toward bulk SiO2.
The total reaction is written as
SiO2 C4eKðthrough Mo or SiÞ Z Si C2O2K
(2)
This novel method might open up a new route for the
high purity Si production. When only oxygen can be
removed from high purity SiO2, Si with similar purity is
produced. This method is especially promising for econ-
omical production of solar grade Si, since SiO2 of solar
grade purity is inexpensive [5]. In order to assess the
possibility of this method, it is important to investigate
the reduction rate and the existence of side reactions. The
reduction rate should be closely related to fO at the three-
2
phase interface, which is controlled by E, as seen from the
Eq. (1). For instance, assuming the initial concentration
level of O2K ion in the melt to be 0.01 mol% and using the
reported DG0f ðCaOð1ÞÞ and DGf0ðSiO2ðsÞÞ [6], reduction of
SiO2 is expected to occur at more negative than 1.21 V (vs.
Ca2C/Ca). Furthermore, it was confirmed that Si–Ca alloy
was formed at negative potential region as a side reaction
[2]. In the present study, therefore, potential dependences of
the reaction and the reduction rate of solid SiO2 in molten
CaCl2 at 1123 K were investigated in detail.
2. Experimental
Fig. 1. Photograph of a SiO2 contacting electrode.
Three hundred grams of CaCl2 (reagent grade, Wako
Pure Chemical Co., Ltd) was contained in a glassy carbon
crucible (10 cm depth, 9 cm inner diameter and 0.2 cm wall
thickness, Tokai Carbon Co., Ltd) and was kept under
vacuum at 473 K for 72 h and at 773 K for 24 h to
remove water. All the experiments were performed under a
dry Ar atmosphere in a sealed stainless steel holder kept at
1123 K.
in distilled water. The compositions of the samples were
analyzed by EPMA (E-MAX ENERGY EX-200, Horiba
Corp.).
3. Results and discussion
A SiO2 contacting electrode shown in Fig. 1 was
prepared by equally winding a Mo wire (f 0.2 mm,
99.95%, Nilaco Corp.) as a current lead, about ten times
around a quartz glass plate (15 mm!5 mm!1 mm, total
metal impurities !1 ppm; NP grade, Tosoh Quartz
Corp.). The counter electrode was a graphite rod
(5 mm!5 mm!20 mm, Tokai Carbon Co., Ltd). The
reference electrode was an AgC/Ag electrode, which was
prepared by immersion of an Ag wire (f 1.0 mm, 99.99%,
Nilaco Corp.) in molten CaCl2 containing 2 mol% AgCl
(99.5%, Wako Pure Chemical Co., Ltd) set in a porous
mullite tube (f 6.0 mm, 3Al2O3$2SiO2, HB grade,
Nikkato Corp.). The potential of this electrode was
calibrated with a reference to that of a Ca2C/Ca electrode
prepared by electrodepositing Ca metal on a Mo wire. All
potentials in this report are given with a reference to this
Ca2C/Ca electrode potential.
3.1. Current–time curves
In our previous study [2], the cyclic voltammogram for a
SiO2 contacting electrode suggested that the electrochemi-
cal reduction of SiO2 occurs at more negative potential than
approximately 1.3 V (vs. Ca2C/Ca), and the reduction to Si
was confirmed at 1.1 V or more negative potential by XRD,
SEM and EPMA. In the present study, to investigate the
reduction between 1.1 and 1.3 V, potentiostatic electrolysis
was conducted at (a) 1.30, (b) 1.25, (c) 1.20, and (d) 1.10 V
for 1 h. Since the reduction rate was considerably higher at
more negative potentials [2], potentiostatic electrolysis was
also carried out at (e) 1.00 and (f) 0.70 V. Moreover,
electrolysis was also conducted at (g) 0.35 V, at which
Si–Ca alloy formation has been confirmed [2], to further
investigate the alloy formation reaction.
Samples were analyzed by XRD (Multiflex 2kW, Rigaku
Fig. 2 shows current–time curves during the electrolysis,
where the cathodic current values are directly correspond to
the reduction rates. At 1.30 V, only residual current was
˚
Corp., Cu Ka line, 1.5418 A) and observed by SEM
(S-2600H, Hitachi) after removing a Mo wire and washing