摘要
温度、SO_2浓度、颗粒大小、石灰石类型和样品的微观结构影响着直接硫酸化反应过程。这一反应过程能用缩芯模型来描述,并对SO_2具有一级反应特征。本征反应和产物层扩散控制反应的活化能分别是85.2kJ/mol和41.5kJ/mol。在800℃、2000ppmSO_2和反应101min的条件下,Igzlaberga和Forsby石灰石的CaCO_3转化率分别可达84%和72%。在初始2min内已煅烧石灰石(CaO)的硫酸化反应速率与石灰石的反应速率稍高,随后二者基本相同。
Temperature, SO_2 concentration,particle size,limestone type and ori-ginal micro structure of sample affect the overall process of direct sulfation. This process can be described by using a shrinking core model .The reaction is found of first order with respect toSO_2.The values of activation energy are 85.2kJ/mol for the intrinsic reaction and 41.5kJ/mol for the reaction controled by the product-lay-er diffusion.At800℃,2000ppm SO_2 and 10 min,the CaCO3 conversion as high as84%and 72%can be expected for Ignaberga and Forsby,respectively,It seems that the sulfation of precalcinedl imestone(CaO)has little faster rate than the direct sulfa-tion of limestone during the first 2 min, and then both have almost same rate.
出处
《重庆环境科学》
1994年第4期5-11,共7页
Chongqing Environmental Science
关键词
石灰石
直接硫酸化反应
缩芯模型
SO2
Thermogravimetric analysis Limestone Direct sulfation Shrinding core model