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Fig. 7 Dependence of initial rate of Zn(II) on ZnCl2 per reaction vial. Each
vial contained 3 mmol ligand, 1 ml TEA, 9 ml MeCN and ZnCl2.
Fig. 6 Relative quinolate concentrations derived from 1H NMR spectra as
300 mM 5,7-dCl-Hq is titrated with ZnCl2 in 9 : 1 MeCN : TEA.
yield is likely due to the limited solubility of ZnCl2, which blocks light
absorption. A first order dependence of the reaction rate on ligand
concentration was also found. The rate of photoreduction initially is
proportional to concentration, but levels off at higher loadings due to
the saturation of light absorption of the photoactive catalyst species.
A R2 value of 0.99 is observed for the logarithmic fit derived from
Beer–Lambert’s law, which indicates that light absorption is satu-
rated at higher catalyst concentrations (ESI†).
To summarize, this work presents the photoreduction of Zn(II)
to zinc metal by a zinc quinolate catalyst that is formed in situ.
The highest yields of zinc metal were obtained using ZnCl2 and
5,7-dichloro-8-hydroxyquinoline in acetonitrile. The active catalyst
was identified as a mono-substituted zinc quinolate by 1H NMR and
luminescence quenching. Future work will focus on the replace-
ment of TEA for nonsacrificial Zn(II) photoreduction. The authors
would like to acknowledge support from the National Science
Foundation through CHE-1055547.
irreversible reduction peak generally observed for Znq2.11 Indeed,
1H NMR of dissolved solids in a typical photoreaction reveal only one
quinolate species, with another-likely the degraded or active catalyst-
forming after light exposure (ESI†). The two other quinolates in Fig. 6
correspond to 5,7-dCl-q and Zn(5,7-dCl-q)2, the latter of which was
synthesized by established procedure for reference purposes.12 The
formation of [Zn(5,7-dCl-q)Ln], and Zn(5,7-dCl-q)2 were reversible;
Keq values of formation were calculated be 1026 MÀ1 and 257 MÀ1
respectively. The parent 5,7-dCl-Hq is fully deprotonated in the TEA
environment and does not absorb 465 nm light, rendering both its
presence and participation in the photoreduction process unlikely.
Fluorescence quenching was employed to confirm that a mono-
substituted zinc quinolate is the active, zinc(II) reducing photo-
catalyst. The sacrificial electron donor TEA is oxidized at +0.934 V
vs. SHE13 and is thus incapable of reducing neither a ground state
zinc quinolate nor unligated Zn(II) directly. As a consequence,
reductive luminescence quenching is necessary. While quenching
by TEA was not detected in 5,7-dCl-q nor Zn(5,7-dCl-q)2, it was
observed in [Zn(5,7-dCl-q)Ln], indicating that it is the active catalyst.
The quenching effect only follows a linear Stern–Vollmer relation-
ship at TEA concentrations below 0.25% v/v and no additional
quenching is observed beyond 1% v/v TEA (ESI†).
Catalyst durability and kinetics were also investigated to gain a
greater understanding of the Zn(II) photoreduction mechanism. It
was found that at 300 mM 5,7-dCl-Hq, Zn(II) reduction largely ceases
after 200 h and fits a first order decay model with R2 = 0.96. After
10 days an average of 242 mmol zinc was produced, equivalent to
81 TONs (ESI†). This constitutes roughly 10% of the Zn present in
the vial and the increasing coating of the vessel with light-blocking
Zn metal could be a contributing factor to this decrease in reactivity.
Rate studies were also performed, and over the first 8 h a
dependence of the zinc production rate on the concentrations of
both ZnCl2 and 5,7-dCl-Hq were measured. Similar to our earlier
work with an Ir(III) catalyst, a minimum concentration of ZnCl2 is
required for the reaction to proceed, represented as the x intercept in
Fig. 7. Interestingly, the x intercept roughly corresponds with the
solubility of ZnCl2 in the reaction mixture, which strongly suggests a
heterogeneous reaction pathway. It can be observed that the initial
reaction rates increase with the addition of more ZnCl2 until it
plateaus and then decreases at very high loadings. This decrease in
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