The TBA salt of polyoxoanion Ni
16L
6(SiW
9)
4 (TBA-Ni
16L
6(SiW
9)
4) was subsequently employed as the molecular catalyst for visible-light-driven hydrogen evolution in a well-established three-component catalytic system using [Ir(coumarin)
2(dtbbpy)]
+ [
53] as the photosensitizer, TEOA as the sacrificial electron donor, and H
2O as the proton source. The photocatalysis was performed in a CH
3CN/DMF (v/v = 1/3) solution under a Xe-lamp light source equipped with a 400 nm cut off filter at 20 ℃. As shown in
Figs. 3a-
c, varying the concentration of each essential component can also greatly adjust the efficiency of H
2 production. For instance, increasing the concentration of TBA-Ni
16L
6(SiW
9)
4 from 0 µmol/L to 25 µmol/L leads to the enhancement of H
2 yield from ~1.98 µmol to ~321.47 µmol in 5 h (
Fig. 3a), corresponding to the TONs of 4619 (5 µmol/L catalyst), 3618 (10 µmol/L catalyst), 3403 (15 µmol/L catalyst), 2677 (20 µmol/L catalyst), and 2143 (25 µmol/L catalyst), respectively (Fig. S5a in Supporting information). The optimized TON (~4619) is calculated at a TBA-Ni
16L
6(SiW
9)
4 concentration of 5 µmol/L, because a given catalyst at relatively low concentration may possibly work as the limiting parameter for reaching a higher TON [
54]. Specifically, during photocatalytic reaction, the photosensitizer is excited to generate photogenerated electrons and holes, which are harvested by TEOA and the catalyst, respectively. When the catalyst concentration is very low, the effective numbers of electrons received by per catalyst become the rate-limiting factor for catalysis, thereby leading to a higher TON value. In other control experiment, turning the concentration of [Ir(coumarin)
2(dtbbpy)]
+ photosensitizer (PS) from 0 to 0.3 mmol/L increased the H
2 yield 64.13 µmol to 162.96 µmol (
Fig. 3b). It is also noted that the increment of TEOA concentration from 0.35 mol/L to 0.50 mol/L does not greatly enhance the H
2 production (
Fig. 3c), indicating that the concentration of TEOA higher than 0.35 mol/L is no longer the rete-limiting factor for photocatalysis. After 5-h photocatalysis, a TON of as high as 6834 has been achieved, which represents one of the highest values in terms of known Ni-substituted POM-catalyzed H
2 production systems (Table S3 in Supporting information). Therefore, an optimal TEOA concentration of 0.35 mol/L is used for further study. To better understand the catalytic system, several control experiments were conducted to assess the importance of each component for photocatalytic hydrogen generation. As shown in
Fig. 3d, the absence of any components (catalyst, sacrificial reagent, or photosensitizer) resulted in negligible hydrogen production, and the optimal photocatalytic system exhibited the highest TON value among various control experiments (Fig. S5b in Supporting information). The catalytic system only produced very little amount of H
2 gas while replacing the TBA-Ni
16L
6(SiW
9)
4 catalyst with TBA-SiW
9, revealing the significance of the Ni active sites. In addition, the replacement of TBA-Ni
16L
6(SiW
9)
4 catalyst with molar equivalents of Ni(NO
3)
2·4H
2O, TBA-SiW
9, and L ligands also led to inefficient H
2 production. These results confirm that the catalyst, photosensitizer, and sacrificial reagent are all indispensable factors, and the special molecular skeleton of TBA-Ni
16L
6(SiW
9)
4 is extremely crucial for efficient photocatalysis.