高浓度含硝酸盐工业废水的催化还原回收铵

IF 4.8 Q1 ENVIRONMENTAL SCIENCES
Dydia Tanisha González, José Alberto Baeza*, Luisa Calvo and Miguel Ángel Gilarranz, 
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引用次数: 0

摘要

近年来,废水处理产生NH4+/NH3并进行回收再利用的概念受到了广泛关注。通过催化还原将废水中的NO3 -转化为NH4+/NH3是一种可持续的废水资源化利用途径。在本工作中,提出了该技术在高浓度NO3 -工业废水中的应用。在高NO3 -浓度下,炭黑负载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, NO3 -完全转化。此外,当反应器不控制pH时,催化活性得到改善,NH4+生成量增加到184 mg/L。此外,在相当于工业废水的反应介质中连续8小时的反应循环中,观察到催化活性逐渐下降,这可能与Pd0/Pdn+物种比明显下降有关。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Catalytic Reduction of High Concentration Nitrate-Bearing Industrial Wastewater for Ammonium Recovery

Catalytic Reduction of High Concentration Nitrate-Bearing Industrial Wastewater for Ammonium Recovery

The concept of NH4+/NH3 production from wastewater treatment for subsequent recovery and reuse has gained much attention in the past few years. The conversion of NO3 present in wastewater into NH4+/NH3 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 NO3 concentration is proposed. A good activity of Pd–Cu catalysts supported on carbon black was observed at high NO3 concentrations. Complete NO3 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 NH4+ 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 Pd0/Pdn+ species ratio.

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CiteScore
5.40
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