A. Kjekshus et al.
ARTICLE
the water-containing medium: CrCl3·6H2O and H(thd) in re- 3.2 Sublimation of Cr(thd)3 and [Cr(thd)2(OEt)]2 Mixtures
fluxing EtOH/H2O. The following scheme is suggested:
The present findings show that sublimation (under com-
Cr3+
+ 3H(thd)(solv.) + 3NH3(solv.) → Cr(thd)3(solv.) + 3NH4 (solv.)(2)
+
monly used conditions) can be a rather laborious way to sepa-
rate Cr(thd)3 and [Cr(thd)2(OEt)]2. There are indeed other
ways based on solvent extraction to perform this task. How-
ever, since reference [2] goes quite far toward recommending
use of sublimation for purification of Cr(thd)3, we will give a
brief account of our experience with the application of subli-
mation on Cr(thd)3/[Cr(thd)2(OEt)]2 mixtures.
(solv.)
Cr(thd)3(solv.) % Cr(thd)3(s)
(3)
(4)
(5)
Cr(thd)3(solv.) + 2EtOH % [Cr(thd)2(OEt)]2(solv.) + 2H(thd)(solv.)
[Cr(thd)2(OEt)]2(solv.) % [Cr(thd)2(OEt)]2(s)
Let us consider two series of experiments, one in which the
sublimation temperature (s.t.) was set at 90 °C and another
with s.t. = 180 °C. The deposition temperature (d.t.; viz. the
temperature at the cold finger) was kept at 50 °C in both series.
The seemingly trivial change of s.t. from 90 to 180 °C caused
a major change in the sublimation process. For the s.t. at 90 °C
series the process commenced with good speed, but soon after
the sublimation rate started to decline, and went asymptotic to
nil. PXD showed that the purple sublimate consisted of
Cr(thd)3. The unsublimed part had become covered at this
stage with a thin layer of green-colored [Cr(thd)2(OEt)]2. Aft-
erwards, the entire batch of unsublimed material was subjected
to gentle crushing and thorough mixing and submitted to re-
newed sublimation treatment. The evolution of the resumed
sublimation process once again followed the course just de-
scribed. In fact, the crushing/mixing-sublimation treatment had
to be repeated about 20 times over two weeks in order to fully
separate Cr(thd)3 from [Cr(thd)2(OEt)]2.
The process at s.t. = 180 °C developed differently. The subli-
mation rate remained largely unaltered during the process, and
the characteristic light green cover-layer on the remnants at the
evaporation source was reduced almost to invisibility. Most of
a 5 g batch of raw material was sublimed after 30 min treat-
ment at 180 °C. PXD of the sublimate after this treatment
showed a mixture Cr(thd)3 and [Cr(thd)2(OEt)]2. This finding
appears to conflict the following statement in reference [2]: “If
the sublimation temperature is maintained near 180 °C, the
light green solid will not sublime at the pressure specified”.
The distinction between the behavior at s.t. = 90 and 180 °C
can be explained by different volatility of Cr(thd)3 and
[Cr(thd)2(OEt)]2. In accordance with its lower molecular mass
and presumably weaker intermolecular van der Waals interac-
tions, Cr(thd)3 obtains a significant sublimation pressure at
lower temperature than [Cr(thd)2(OEt)]2. This concurs with the
fact that [Cr(thd)2(OEt)]2 is detected in the sublimates from
the 180 °C series, but absent in the 90 °C series.
As also established in reference [2], [Cr(thd)2(OEt)]2 is less
soluble in EtOH/H2O than Cr(thd)3 and this is evidently the
cause of its appearance as a minor phase in the product mix-
ture. The balance between the constituents of the product is in
any case regulated through Equations (2)–(5). The reversibility
of Equation (4) was tested by heating 1:2 stoichiometric mix-
tures of [Cr(thd)2(OEt)]2 and H(thd) dissolved in (i) EtOH/
H2O, (ii) abs. EtOH, and (iii) H(thd) heated to reflux. The
experiments with EtOH/H2O as solvent turned out somewhat
inconclusive. A faint red coloring of the liquid phase indicated
that the anticipated reaction had commenced, but the process
had then discontinued. This is in agreement with poor solubil-
ity of [Cr(thd)2(OEt)]2 in EtOH/H2O.
[Cr(thd)2(OEt)]2 is obtained from Cr(thd)3 and EtOH accord-
ing to the forward direction of Equation (4) [solv. here denot-
ing abs. EtOH; 5 d heating to reflux gave ca. 5 wt.-%
[Cr(thd)2(OEt)]2 and 95 wt.-% unreacted Cr(thd)3]. Since
[Cr(thd)2(OEt)]2 dissolves poorly in abs. EtOH, the absence of
the reverse reaction is in accordance with expectations. How-
ever, the reversibility of Equation (4) was ascertained by the
use of H(thd) as both reactant and solvent. For example, heat-
ing a mixture of [Cr(thd)2(OEt)]2 and H(thd) to reflux for one
day gave (semi-quantitatively assessed) Cr(thd)3 in amounts
corresponding to the proportions of the starting mixtures.
An essential inference from the present study is the confir-
mation of the reversibility of Equation (4), which in turn is
controlled [Equation (3) and (5)] by the relative solubilities of
Cr(thd)3 and [Cr(thd)2(OEt)]2 in the solvent concerned. The
basis for the inevitable occurrence of Cr(thd)3/[Cr(thd)2(OEt)]2
mixtures in synthesis according to the urea-based recipe of ref-
erence [2] is laid by use of water-containing ingredients. The
relative amounts in the product mixtures can to some extent
be changed, but since H2O has to be present according to
Equation (1), both complexes should appear in the product.
However, turning to water-free ingredients phase-pure
[Cr(thd)2(OEt)]2 can be prepared according to:
The participation of sublimation of [Cr(thd)2(OEt)]2 in the
s.t. = 90 °C series is manifested as the thin green cover-layer
on the source material, which gradually renders evaporation of
Cr(thd)3 difficult and eventually blocks the sublimation proc-
2CrCl3(solv.) + 6Na(OEt)(solv.) + 4H(thd)(solv.)
[Cr(thd)2(OEt)]2(s) + 4EtOH + 6NaCl(s)
→
(7)
The introduction of Na(OEt) from the very beginning makes ess. Even though both complexes are volatile at 90 °C, the
the use of urea and thus Equations (1) and (2) become super- sublimation pressure of [Cr(thd)2(OEt)]2 is low and the flight
fluous. With CrCl3 and H(thd) as other reactants and abs. EtOH range is short. At onset, the Cr(thd)3 at the evaporation source
as solvent, [Cr(thd)2(OEt)]2 is obtained phase-pure in about has large surface areas free for [Cr(thd)2(OEt)]2, viz. numerous
93 % yield. This approach mimics the synthesis of locations are accessible for sublimation. However, some
[Cr(thd)2(OMe)]2 [4] and preparation of the last mentioned [Cr(thd)2(OEt)]2 will also become vaporized, but for s.t. =
complex was repeated (some 90 % yield) according to the 90 °C these species cannot travel far from their original loca-
presently modified procedure.
tion and they will eventually deposit on available colder spots
© 2011 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim
Z. Anorg. Allg. Chem. 2011, 56–61