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Ultrasound-Enhanced Catalytic Ozonation Oxidation of Ammonia in Aqueous Solution

机译:超声强化水溶液中氨的催化臭氧氧化

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摘要

Excessive ammonia is a common pollutant in the wastewater, which can cause eutrophication, poison aquatic life, reduce water quality and even threaten human health. Ammonia in aqueous solution was converted using various systems, i.e., ozonation (O3), ultrasound (US), catalyst (SrO-Al2O3), ultrasonic ozonation (US/O3), ultrasound-enhanced SrO-Al2O3 (SrO-Al2O3/US), SrO-Al2O3 ozonation (SrO-Al2O3/O3) and ultrasound-enhanced SrO-Al2O3 ozonation (SrO-Al2O3/US/O3) under the same experimental conditions. The results indicated that the combined SrO-Al2O3/US/O3 process achieved the highest NH4+ conversion rate due to the synergistic effect between US, SrO-Al2O3 and O3. Additionally, the effect of different operational parameters on ammonia oxidation in SrO-Al2O3/O3 and SrO-Al2O3/US/O3 systems was evaluated. It was found that the ammonia conversion increased with the increase of pH value in both systems. The NH3(aq) is oxidized by both O3 and ·OH at high pH, whereas the NH4+ oxidation is only carried out through ·OH at low pH. Compared with the SrO-Al2O3/O3 system, the ammonia conversion was significantly increased, the reaction time was shortened, and the consumption of catalyst dosage and ozone were reduced in the SrO-Al2O3/US/O3 system. Moreover, reasonable control of ultrasonic power and duty cycle can further improve the ammonia conversion rate. Under the optimal conditions, the ammonia conversion and gaseous nitrogen yield reached 83.2% and 51.8%, respectively. The presence of tert-butanol, CO32−, HCO3, and SO42− inhibited the ammonia oxidation in the SrO-Al2O3/US/O3 system. During ammonia conversion, SrO-Al2O3 catalyst not only has a certain adsorption effect on NH4+ but accelerates the O3 decomposition to ·OH.
机译:氨是废水中的常见污染物,会导致富营养化,污染水生生物,降低水质甚至威胁人体健康。使用各种系统转换水溶液中的氨,这些系统包括臭氧化(O3),超声(US),催化剂(SrO-Al2O3),超声臭氧化(US / O3),超声增强的SrO-Al2O3(SrO-Al2O3 / US) ,SrO-Al2O3臭氧化(SrO-Al2O3 / O3)和超声增强SrO-Al2O3臭氧化(SrO-Al2O 3 / US / O 3 ) 。结果表明,SrO-Al 2 O 3 / US / O 3 工艺组合获得最高的NH 4 2 O 3 和O 3 之间的协同作用,导致> + 转化率。另外,不同操作参数对SrO-Al 2 O 3 / O 3 和SrO-Al 2中氨氧化的影响评估 O 3 / US / O 3 系统。发现在两个系统中氨转化率都随着pH值的增加而增加。 NH 3 (aq)在高pH下被O 3 和·OH氧化,而NH 4 + 氧化仅在低pH下通过·OH进行。与SrO-Al 2 O 3 / O 3 体系相比,氨转化率显着提高,反应时间缩短, SrO-Al 2 O 3 / US / O 3 系统降低了催化剂用量和臭氧消耗。此外,合理控制超声功率和占空比可以进一步提高氨转化率。在最佳条件下,氨转化率和气态氮产率分别达到83.2%和51.8%。叔丁醇,CO 3 2-,HCO 3 -和SO 4的存在 2-抑制SrO-Al 2 O 3 / US / O 3 系统。氨气转化过程中,SrO-Al 2 O 3 催化剂不仅对NH 4 + 有一定的吸附作用。但会加速O 3 分解为·OH。

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