González Dydia Tanisha, Baeza José Alberto, Calvo Luisa, Gilarranz Miguel Ángel
Departamento de Ingeniería Química, C/Francisco Tomás y Valiente 7, Universidad Autónoma de Madrid, 28049 Madrid, Spain.
Institute for Advanced Research in Chemical Sciences (IAdChem), Universidad Autónoma de Madrid, 28049 Madrid, Spain.
ACS ES T Water. 2025 Mar 20;5(4):1595-1604. doi: 10.1021/acsestwater.4c00897. eCollection 2025 Apr 11.
The concept of NH /NH production from wastewater treatment for subsequent recovery and reuse has gained much attention in the past few years. The conversion of NO present in wastewater into NH /NH through catalytic reduction is a sustainable approach for resource utilization from wastewater. In the present work, the application of this technique to industrial wastewater with a high NO concentration is proposed. A good activity of Pd-Cu catalysts supported on carbon black was observed at high NO concentrations. Complete NO conversion was achieved in water with an initial concentration of 1000 mg/L and a catalyst concentration of 0.93 g/L in a stirred reactor. Furthermore, an improvement in catalytic activity was obtained when the reactor was operated without pH control, resulting in an increase in NH formation to 184 mg/L. Additionally, in successive 8-h reaction cycles with a reaction medium equivalent to that of industrial wastewater, a progressive decrease in catalytic activity was observed, which may be associated with a noticeable decrease in the Pd/Pd species ratio.
在过去几年中,通过废水处理产生氨氮用于后续回收和再利用的概念备受关注。通过催化还原将废水中存在的硝酸盐转化为氨氮是一种可持续的废水资源利用方法。在本工作中,提出了将该技术应用于高硝酸盐浓度的工业废水。在高硝酸盐浓度下观察到负载在炭黑上的钯 - 铜催化剂具有良好的活性。在搅拌反应器中,初始浓度为1000 mg/L的水中,催化剂浓度为0.93 g/L时实现了硝酸盐的完全转化。此外,当反应器在不控制pH的情况下运行时,催化活性得到改善,氨氮生成量增加至184 mg/L。此外,在与工业废水反应介质相当的连续8小时反应循环中,观察到催化活性逐渐降低,这可能与钯/钯物种比率的显著降低有关。