Electrocatalytic reduction of nitrate (NO 3 − ) to ammonia (NH 3 ) (NO 3 RR) coupled with NH 3 separation represents a sustainable approach to mitigate nitrate pollution and recycle nitrogen from contaminated water. Nevertheless, this process is deemed impractical for contaminated natural water bodies owing to the limited presence of NO 3 − −N (<50 mg L −1 ) and electrolytes and the relative abundance of scaling ions (Mg 2+ and Ca 2+ ). Furthermore, copper (Cu), as the primary NO 3 RR catalyst, generally suffers from NO 2 − accumulation and a prevalence of side hydrogen evolution. Herein, we develop an integrated system comprising sections of NO 3 − enrichment and NO 3 RR and NH 3 collection, alongside a single-atom Cu-bearing CeO 2 catalyst (Cu 1 / CeO 2 ) for NO 3 RR. With this system, diluted NO 3 − is extracted from contaminated water using anion-exchange resins and then released into a concentrated NaCl aqueous solution, providing a solution with ample NO 3 − −N (∼822 mg L −1 ) and electrolytes (∼1.7 M NaCl) while being free of scaling ions. Within this solution, the Cu 1 /CeO 2 demonstrates an exceptional high and steady NH 3 −N production rate of 7.8 g NHd 3 −N g Cu −1 h −1 , an NH 3 −N selectivity of 90.1%, and a Faradaic efficiency of 91.3%, outperforming the Cu nanoparticles (1.8 g NHd 3 −N g Cu −1 h −1 , 46.3%, and 53.0%). In situ experiments and theoretical computations reveal a dual-site NO 3 RR mechanism involving the electron-deficient Cu 1 site and adjacent oxygen vacancies, which collaborate to promote NO 3 − adsorption and lower conversion barrier while inhibiting hydrogen evolution. Finally, we implemented the integrated system along the Yangtze River, achieving nitrate elimination and nitrogen recycling with a competitive energy consumption of 1.36−1.54 kW h mol N −1