“…[ 3,4 ] However, traditional carbon electrodes exhibit poor desalination capacity (less than 20 mg NaCl g −1 ) and sluggish rate capability (slower than 1 mg NaCl g −1 min −1 ). [ 5 ] Other non‐carbon candidates, including transition metal oxide (e.g., TiO 2 , Na x MnO 2 , V 2 O 5 , MnO 2 ), [ 6,7,8 ] Prussian blue analogs (e.g., Na 2 CoFe(CN) 6 , FeFe(CN) 6 , Na 2 CuFe(CN) 6 ), [ 9,10 ] polyanionic phosphates (e.g., amorphous FePO 4 , NaTi 2 (PO 4 ) 3 , Na 3 V 2 (PO 4 ) 3 ), [ 11,12 ] MXenes (e.g., Ti 3 C 2 T x ), [ 13 ] and transitional metal dichalcogenides (e.g., MoS 2 , TiS 2 ), [ 8,14 ] usually suffer from high material cost, low intrinsic conductivity, and poor cycling durability resulting from significant volume change, leading to being far from practical application in CDI process. As a consequence, it is very urgent to exploit high‐performance electrodes for advancing CDI systems.…”