Traditional homogeneous Fenton catalysis process can degrade most organic pollutants [
144]. However, the drawbacks of narrow work pH range, accumulation of ferric oxide sludge, and low H
2O
2 utilization rate significantly limit its wide-spread application [
145]. In recent years, the heterogeneous Fenton-like catalysis-based SACs with high catalytic activities and a wide work pH range has been developed [
12,
110,
121,
137-
139],
146,
147]. Zhou and co-authors prepared the Fe
SA-N-C for efficient catalytic oxidation of bisphenol A (BPA)
via peroxymonosulfate (PMS) activation [
137]. 100% removal of BPA (20 mg/L) could be observed in 30 min for Fe
SA-N-C/PMS (0.15 g/L Fe
SA-N-C and 0.4 g/L PMS), which was higher than that of Fe
NP-N-C/PMS, indicating the unique catalytic activity of the single Fe sites. The Fe content in the Fe
SA-N-C could affect the catalytic activity for BPA degradation, and the Fe
SA-N-C-20 (20 mg Fe (NO
3)
3·9H
2O) showed remarkable performance for PMS activation because it has a large number of Fe-N
x active sites. Zhang
et al. synthesized the FeCo-NC at different calcination temperatures, and found that the FeCo-NC-2 (calcined at 650 ℃) showed the highest performance for PMS activation [
12]. For FeCo-NC-2, the 100% removal of BPA (20 mg/L) could be observed in 4 min (0.1 g/L FeCo-NC-2 and 0.2 g/L PMS). Zhu
et al. synthesized a Co-N-C catalyst for activating PMS [
121]. They found that the Co-N-C calcined at 900℃ could completely remove BPA (80 mg/L) in 3 min (0.5 g/L Co-N-C-900 and 0.3 g/L PMS). Chen
et al. prepared the SA-Cu/rGO for the degradation of SMX (sulfamethoxazole) by activating PMS [
138]. The degradation kinetic of the SA-Cu/rGO/PMS was about 3.9 times faster than that of the rGO/PMS. The SA-Cu/rGO/PMS system showed very high mineralization ability because over 99% of the TOC was eliminated within 120 min. Apart from this, a dual reaction sites SAC was prepared for PDS activation and organics decomposition in Shang's article [
148]. SMX would be well adsorbed
via benzene ring binding for the abundant conjugated
π-
π sp
2 structured carbon and the Fe-N
4 sites also has strong binding adsorption to PDS. The adsorption of SMX is beneficent to minimize the migration distance of the ROS. Meanwhile, PDS activation is accelerated due to the combined between Fe-N
4 sites and PDS molecular. Because of this, the organics decomposition process of the reconstructed Fe-SAC is significantly higher (~6 times) than the conventional Fe-SAC (
Fig. 7a). In another research, a SAC-based PMS system was used to the degradation of bisphenol A (BPA) and metronidazole (MNZ) [
149]. Radical oxidation (SO
4•− and HO
•) and nonradical electron transfer pathway (ETP) all co-existed in the Co−N
4−C/PMS system according to the quenching experiments. From density functional theory calculations, the Co-N
4 active sites increased the adsorption and activation of PMS which improve the charge transfer to PMS to evolve radicals. A Fe-SAC located on carbon nitride used in flow-through filter was reported by Professor Zhang [
150]. With the FeCN
5 activate sites and ultrafast H
2O
2 activation, methylene blue oxidation rate can reach to 59.43 mg L
−1 min
−1 via direct and nearly 100% pollutant degradation and stability over 320 h in actual wastewater solution (
Fig. 7b). For comparison, Xiong and co-workers found that the removal rate constant of
p-nitrophenol (PNP) by micro zero-valent was 0.1779 min
−1 [
151]. Liang [
152] and team-workers investigated catalytic activity of Co-SACs from the coordination number. They found that the coordination N with metal single atom could modulate electron distribution and the decrease of nitrogen coordination number will lead to higher specific activity of Co-N
x.