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结晶法由硫辛酸厂含铝废水制备铵明矾
引用本文:黄燕华,王建浩,姚志远,宋国强,曾桂凤,周永生,顾玥,王车礼.结晶法由硫辛酸厂含铝废水制备铵明矾[J].过程工程学报,2013,13(3):436-441.
作者姓名:黄燕华  王建浩  姚志远  宋国强  曾桂凤  周永生  顾玥  王车礼
作者单位:常州大学石油化工学院 常州大学制药与生命科学学院 常州大学石油化工学院 常州大学制药与生命科学学院 常州大学石油化工学院 常州大学制药与生命科学学院 常州大学石油化工学院
基金项目:江苏省科技厅省级工程技术研究中心资助项目(编号:BM2012416);江苏省“青蓝工程”中青年学术带头人资助项目(编号:QLG02020002)
摘    要:以硫辛酸厂含铝废水中的Al3+为原料,采用结晶法制备铵明矾,研究了时间、NH4+/Al3+摩尔比、SO42-/Al3+摩尔比、温度、搅拌速度对废水中铝去除率和铵明矾产量的影响,对所制铵明矾与商品铵明矾进行比较. 结果表明,两者具有几乎相同的晶体结构、形貌和化学组成,所得产品符合同类工业产品标准. 结晶法用硫辛酸厂含铝废水制备铵明矾的适宜条件为:反应时间8 h,NH4+/Al3+ 1.40,SO42-/Al3+ 2.90,温度5~15℃,搅拌速度35~55 r/min. 宏观反应动力学表明,在晶体生长期,Al3+在边界层扩散传质为反应控制步骤,液相主体Al3+浓度C随时间t的变化关系符合方程C=(C0-Ci)e-kt+Ci. 当搅拌速度较低时,铵明矾晶体平均粒径大,分布宽;搅拌速度增加,晶体平均粒径减小,粒径分布变窄.

关 键 词:铵明矾  硫辛酸  含铝废水  反应结晶  动力学  
收稿时间:2013-1-21
修稿时间:2013-4-8

Synthesis of Ammonium Alum from Lipoic Acid Plant Wastewater by Crystallization
HUANG Yan-hua,WANG Jian-hao,YAO Zhi-yuan,SONG Guo-qiang,ZENG Gui-feng,ZHOU Yong-sheng,GU Yue,WANG Che-li.Synthesis of Ammonium Alum from Lipoic Acid Plant Wastewater by Crystallization[J].Chinese Journal of Process Engineering,2013,13(3):436-441.
Authors:HUANG Yan-hua  WANG Jian-hao  YAO Zhi-yuan  SONG Guo-qiang  ZENG Gui-feng  ZHOU Yong-sheng  GU Yue  WANG Che-li
Affiliation:1 (1. School of Petrochemical Engineering, Changzhou University, Changzhou, Jiangsu 213164, China; 2. School of Pharmaceutical Engineering and Life Science, Changzhou University, Changzhou, Jiangsu 213164, China)
Abstract:Aluminum-containing wastewater was used to synthesize ammonium alum by crystallization. The effects of time, NH4+/Al3+ molar ratio, SO42-/Al3+ molar ratio, temperature and stirring speed on the aluminum alum formation and aluminum ion removal rate were studied. The synthesized and commercial ammonium alum products were characterized, they had almost identical crystal structure, morphology and chemical composition. The optimum conditions of efficient crystallization process were recommended: operation time of 8 h, NH4+/Al3+ of 1.40, SO42-/Al3+ of 2.90, temperature of 5~15℃ and stirring speed of 35~55 r/min. The synthesis reaction kinetics experiments were performed. The results show that Al3+ diffusion in the boundary layer is the rate controlling step in the crystallization process. The relationship between Al3+ concentration (C) and time (t) is expressed by C=(C0-Ci)e-kt+Ci. The effect of stirring speed on the particle size distribution of ammonium alum crystals was investigated. When the stirring speed is lower, ammonium alum average particle size is larger and size distribution wider. With increasing of stirring speed, the particle size and distribution range are decreased.
Keywords:ammonium alum  lipoic acid  wastewater containing aluminum  reactive crystallization  kinetics  
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