首页|撞击流反应器脱除硫酸尾气中SO2的研究

撞击流反应器脱除硫酸尾气中SO2的研究

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采用钠-钙双碱法在撞击流气液反应器中脱除硫酸尾气中的SO2,探讨了模拟硫酸尾气中SO2质量浓度、吸收液NaOH质量分数、液气比和雾化压力等因素对脱硫效率的影响.研究表明:当模拟硫酸尾气中SO2质量浓度越低、吸收液NaOH质量分数越高、液气比和雾化压力越高时,脱硫率越高.当模拟硫酸尾气中SO2质量浓度在800-2400 mg/m3范围内时,优化得到的脱硫工艺条件为:吸收液NaOH质量分数为2.0%,液气比为0.34-0.36 L/m3,对应雾化压力为1-1.2 MPa.在此条件下,脱硫率可高于97%,其脱硫后尾气SO2质量浓度小于100 mg/m3,远低于GB26132-2010规定的排放标准.
Removal of sulfur dioxide in the sulfuric acid tail gas in impinging stream gas-liquid reactor
The sodium-calcium double alkali method was used to remove sulfur dioxide in sulfuric acid tail gas in impinging stream gas-liquid reactor.The effects of the SO2 mass concentration of simulated sulfuric acid tail gas,the NaOH mass fraction of absorbent,liquid-gas ratio and atomization pressure on desulfurization rate were investigated.The results show that with the lower SO2 mass concentration,the higher NaOH mass fraction,the higher liquid-gas ratio and atomization pressure,the desulfurization rate is higher.When the SO2 mass concentration of simulated sulfuric acid tail gas is between 800 and 2400 mg/m3,the optimized conditions for impinging stream gas-liquid reactor removing sulfur are as follows:the absorption liquid NaOH mass fraction is 2.0%,the liquid and gas ratio is 0.34-0.36 L/m3,the atomization pressure is 1-1.2 MPa.Under above conditions,the desulfurization rate is above 97%,the SO2 mass concentration of the tail gas is below 100 mg/m3,which is far lower than the emission standard stipulated by GB26132-2010.

double alkali methodsulfur dioxideimpinging stream gas-liquid reactorsulfuric acid tail gas

周玉新、曲志鹏、熊伟、郭嘉

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武汉工程大学 化工与制药学院 绿色化工过程省部共建教育部重点实验室,湖北武汉430073

双碱法 二氧化硫 气液撞击流反应器 硫酸尾气

国家自然科学基金资助项目

21076165

2016

化学工程
华陆工程科技有限责任公司

化学工程

CSTPCDCSCD北大核心
影响因子:0.438
ISSN:1005-9954
年,卷(期):2016.44(4)
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