程序升温热解磷酸氨镁及热解产物的氨氮脱除性能（英文）

Temperature-programmed pyrolysis of magnesium ammonium phosphate and removal of ammonia-nitrogen by its pyrolysate

为使磷酸氨镁(MAP)脱氨完全及改善热解产物的氨氮去除性能,研究了一种程序升温的热解方式,并探讨了热解产物去除氨氮的热力学及动力学过程。结果表明,热解方式及热解终点温度明显影响MAP热解产物的氨氮去除性能,控制热解终点温度为180°C、5°C/min的程序升温方式,以及氨氮反应体系的p H值为9.5较为合适,在此条件下,MAP热解产物对氨氮的去除量达95.62 mg/g,经120 min对起始浓度为1000 mg/L氨氮的去除率达82%;动力学及热力学结果表明,MAP热解产物去除氨氮是H^+与NH_4^+的离子交换过程,其动力学符合Lagergren准二级模型,平衡时间为120 min,等温曲线符合Freundlich模型。

In order to achieve the dual goals of complete deamination of magnesium ammonium phosphate（MAP） and ensure the pyrolysate＇s good removal properties towards ammonia-nitrogen, a temperature-programmed method for the pyrolysis of MAP was studied, as well as the thermodynamic and kinetic processes involved in the removal reaction system between MAP pyrolysate and aqueous ammonium. It was found that the pyrolysis method and pyrolysis final temperature had significant effects on the MAP pyrolysate＇s removal properties towards aqueous ammonium, and the following conditions were deemed to be more appropriate： pyrolysis final temperature and heating rate at 180 ℃ and 5 ℃/min, respectively, and a pH level of 9.5 for the removal reaction system. The resultant ammonium removal capacity by the MAP pyrolysate was 95.62 mg/g. After 120 min, the removal rate with an initial concentration of 1000 mg/L was 82%. The kinetic and thermodynamic results indicated that the removal of aqueous ammonium by MAP pyrolysate was the exchange process between H^＋ and NH4^＋ via MAP precipitation. The kinetics complied with the Lagergren quasi second-order model with an equilibrium time of 120 min, while the isothermal curves complied with the Freundlich model.