结晶
成核
过饱和度
诱导期
镁
活化能
动力学
晶体生长
试剂
化学
Crystal(编程语言)
氢氧化物
无机化学
化学工程
材料科学
结晶学
物理化学
有机化学
催化作用
物理
量子力学
计算机科学
程序设计语言
工程类
作者
Lijuan Lu,Quanxian Hua,Jianwei Tang,Yong Liu,Li Liu,Baoming Wang
标识
DOI:10.1002/crat.201700130
摘要
Abstract Magnesium hydroxide (Mg(OH) 2 ) is an important chemical raw material and product. Since narrow crystal size distribution of Mg(OH) 2 determines its excellent physical and chemical properties, gaining insight into the reactive crystallization kinetics of Mg(OH) 2 to obtain narrow particle size distribution is essential. The reactive crystallization kinetics of Mg(OH) 2 for the Mg(NO 3 ) 2 ‐NaOH system is systematically investigated during batch crystallization. The effects of supersaturation and temperature on the reactive crystallization kinetics of Mg(OH) 2 are studied. Ion concentration over crystallization time at different temperatures is measured by the conductivity method so that the induction period is well defined. Several kinetic parameters during the nucleation and growth process are determined by using the experimental data of ion concentration over crystallization time at different temperatures. Results show that the induction period decreases with increase of temperature and initial reagent concentration. The specific surface Gibbs energy decreases with the increase of temperature. Crystallization rate increases with increase of temperature and initial reagent concentration, and the nucleation and crystal growth rates can be described as the first order reaction model.
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