1
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Y.-H. Sun et al. / Journal of Alloys and Compounds 413 (2006) 175–180
The CVT or SC-CVT mutual separation for the lanthanide
elements showed that the ionic radius difference of two
elements is one of the decisive factors for the separation
efficiency [1–12,15–17,19,21,22], and the separation for Sc
and Y from Sc2O3–La2O3 [13], Y2O3–La2O3 [13,18,20],
Y2O3–Nd2O3 [18,20], Y2O3–Sm2O3 [18,20], Y2O3–Dy2O3
2. Experimental details
The chemicals used in this study were analytic purity for
KCl, active carbon powder and ≥99.9% purity for all rare
earth oxides. A raw mixture was formed by mixing active
carbon and KCl with a binary oxide mixture of rare earth ele-
ꢀ
ꢀ
[14,22], Y2O3–Ho2O3 [14,21], Y2O3–Er2O3 [14,22] and
ments Ln and Ln at an atomic ratio of C:Ln:Ln :K = 6:1:1:1,
which contains 3.0–5.0 mmol of each rare earth element, Ln
Ho2O3–Sc2O3 [21] showed that the ionic structure and the
electronic configuration are the key factors in the CVT reac-
tion.
Recently, Wang’s group has determined the thermody-
namic properties of the gaseous species LnAlnCl3n+3 for
all of rare earth elements including Sc and Y, and found
that LnAl3Cl12 is the predominant gaseous complex species
for the lanthanide series from La to Lu [24–26] while
LnAl2Cl9 for Sc and Y [23] in the temperature range from
ꢀ
and Ln .
The SC-CVT reaction was carried out in a cylindrical
alumina reactor tube, 25 mm inner diameter and 1000 mm
length, with a given temperature gradient as described in
previous paper [10–12,15–22]. Let T denote the highest tem-
perature in the tube reactor, where the raw materials were
placed. The raw material was chlorinated by dry Cl gas with
2
3
−1
a flow rate of 20 cm min at T = 800 K for 2 h. The Cl gas
2
5
00 to 900 K. On the other hand, Adachi and co-workers
2
was replaced by a dry Ar–Cl mixed gas with the flow rates
of 30 and 10 cm min , respectively, within the tempera-
3
−1
[13,14] have reported the CVT characteristics of the binary
oxide mixtures Sc2O3–Y2O3 [13], Sc2O3–La2O3 [13]
and Y2O3–Ln2O3 (Ln = La [13], Dy [14], Ho [14] and Er
ture range of T = 800–1300 K. Then, the rare earth chlorides
reactedwithKCltoformthevaporcomplexesKLnCl , which
4
[14]) mediated by gaseous complexes LnAlnCl3n+3 and
were transported chemically along the temperature gradient
KLnCl4. The experiment results [13,14] indicated that ScCl3
could be easily separated from YCl3 and LaCl3 while the
unexpected results that the lowest CVT efficiency and the
lowest gaseous complexes stability for YCl3 compared with
LnCl3 (Ln = Dy, Ho and Er) were observed. Very recently,
we [18,20–22] reported the mutual separation characteristics
for Sc, Y, Ho and lanthanoid rare earth elements, such as
La, Nd, Sm, Dy and Er from their binary oxide mixtures
Sc2O3–Y2O3 [18,20], Y2O3–Ln2O3 (Ln = La [18,20], Nd
in the tube reactor at T = 1300 K for 6 h with the Ar–Cl car-
rier gas. At the end of each run, the amounts of the rare earth
2
chloride produced were determined from the peak intensity of
3+
the characteristic bands: 337.271 nm for Er , 337.215 nm for
3
+
3+
3+
Sc , 377.433 nm for Y , 333.749 nm for La , 401.225 nm
3+
3+
3+
for Nd , 359.260 nm for Sm , 342.247 nm for Gd and
339.898 nm for Ho , on an inductively coupled plasma
atomic emission spectrometry (Perkin-Elmer, Optima 2000).
3+
[18,20], Sm [18,20], Dy [22], Ho [21,22] and Er [22]),
Sc2O3–Ho2O3 [21] and Ho2O3–Ln2O3 [21] (Ln = Y,
La, Nd and Sm) using SC-CVT reaction mediated by
LnAlnCl3n+3 [18] and KLnCl4 [20–22]. The results mainly
show the largest total transport yields of YCl3 compared
with that of Sc, La, Nd and Sm mediated by LnAlnCl3n+3,
that is YCl3 > NdCl3 > SmCl3 > LaCl3 > ScCl3 [18] while
3. Results and discussion
3.1. Mutual separation for Er2O3–Ln2O3 (Ln = Sc, Y,
La, Nd, Sm, Gd and Ho)
Fig. 1(A–G) show the SC-CVT reaction results of
the binary oxide mixtures Er2O3–Sc2O3, Er2O3–La2O3,
Er2O3–Nd2O3, Er2O3–Sm2O3, Er2O3–Gd2O3 determined
in this study, together with those of Er2O3–Y2O3 [22] and
Er2O3–Ho2O3 [22], in the form of deposition profiles for the
rare earth chlorides transported versus fraction numbers (FN)
of the receptors, taking KCl as complex former and Argon
gas as carried gas in the given temperature gradient for 6 h.
It can be seen that there are few ScCl3 deposited in the
receptor from FN = 1–7, and only a very small amounts of
ScCl3 concentrates in the lower temperature region from
1050 to 900 K (FN = 8–12) indicated that the vapor com-
plexes KScCl4 is stable in the higher temperature range and
decomposed only in the lower temperatures region, while
ErCl3 mainly distributes in the middle temperature range
from 1120 to 980 K (FN = 5–10). For Er–Y system [22],
the main distribution temperature of both ErCl3 and YCl3
concentrated in 1000–750 K (FN = 9–14). For lanthanoid
elements Er–Ln (Ln = La, Nd, Sm, Gd and Ho [22]), the
distribution of chlorides was in accordance with the ionic
NdCl3 > SmCl3 > LaCl3 > YCl3 > ScCl3
mediated
by
KLnCl4 [20], and that of LaCl3 > HoCl3 > NdCl3 > SmCl3 >
YCl3 > ScCl3 [21] and HoCl3 > ErCl3 > DyCl3 > YCl3 [22]
mediated by KLnCl4. Moreover, Sc and La are easily
separated from Y and Ho compared with the other elements.
Generally, the chlorination ability of Er2O3 is as low
as that of Ho2O3 and Y2O3 under normal chlorination
conditions, since the ionic radius of erbium is very similar
to that of holmium and yttrium. So, the chemical vapor
transport characteristics of Er2O3–Ln2O3 should be close
to that of Y2O3–Ln2O3 [18,20] and Ho2O3–Ln2O3 [21]
mediated by vapor complexes LnAlnCl3n+4 or KLnCl4.
Thus, in this study, together with those shown in [22] for
Er2O3–Y2O3 and Er2O3–Ho2O3, we tried to systematic
investigate the mutual separation characteristics for Er, Sc,
Y, La, Nd, Sm, Gd and Ho from their binary oxide mixtures
Er2O3–Sc2O3, Er2O3–Y2O3, Er2O3–La2O3, Er2O3–Nd2O3,
Er2O3–Sm2O3, Er2O3–Gd2O3 and Er2O3–Ho2O3 using
SC-CVT reaction mediated by KLnCl4.