首页> 外文期刊>Fuel >Experimental and modelling analysis of seawater scrubbers for sulphur dioxide removal from flue-gas
【24h】

Experimental and modelling analysis of seawater scrubbers for sulphur dioxide removal from flue-gas

机译:海水洗涤塔去除烟气中二氧化硫的实验和模型分析

获取原文
获取原文并翻译 | 示例
           

摘要

Scrubbing with seawater is a reliable technology for flue-gas desulfurization in coal-fired power plants or in marine applications. The introduction of new regulations for emission control in Europe and the due increment of operational efficiency are pushing forward the optimization of scrubber's design, for which packing columns may be a better solution compared to spray columns. The design of a seawater scrubber mainly relies on a correct assessment of the equilibrium conditions and of the mass transfer coefficients in the absorber. In this work, experiments are performed on a model flue-gas (32 m(3).h(-1)) having a SO2 concentration in the range 500-2000 ppm(v), treated in a packed column filled with a structured packing (Mellapak 250X (R)) at 1 atm and 25 degrees C, with liquid-to-gas ratio between 1.06 and 3.44 kg.kg(-1). Three different absorbing solutions are investigated: (a) a seawater; (b) a basic solution obtained by adding 200 mg.L-1 NaOH solution to the seawater and (c) distilled water, used as benchmark. In order to analyze the packed column tests, SO2 equilibrium absorption tests at low concentrations (100-2000 ppmv) are carried out in a feed-batch reactor, using the same absorbing solutions tested in column tests. The experimental tests in packed column indicate that, for SO2 concentration as low as 500 ppm, an absorption efficiency above 98% can be achieved by using liquid-to-gas mass ratio about to 2.91 kg.kg(-1). In this condition, few differences appear among solutions (a) and (b). For the highest SO2 concentration (i.e. 2000 ppmv), a maximum of 85% efficiency is observed for liquid-to-gas mass ratio of 3.44 kg.kg(-1). Modeling of both the equilibrium and the dynamic data are implemented in Aspen Plus (R) V 8.6. However, while modeling assures a very good prediction of the equilibrium data, it is not able to properly describe the dynamic test results, with a systematic underestimation for tests having a removal efficiency higher than 85%.
机译:海水洗涤是燃煤电厂或海洋应用中烟气脱硫的可靠技术。欧洲新的排放控制法规的出台以及运营效率的适当提高推动了洗涤塔设计的优化,与喷雾塔相比,填料塔可能是更好的解决方案。海水洗涤塔的设计主要取决于对吸收塔中平衡条件和传质系数的正确评估。在这项工作中,对烟道气中的SO2浓度在500-2000 ppm(v)范围内的模型烟气(32 m(3).h(-1))进行了实验,并在填充有结构化填料的填充塔中进行了处理。填料(Mellapak 250X(R))在1个大气压和25摄氏度的温度下进行,液/气比在1.06和3.44 kg.kg(-1)之间。研究了三种不同的吸收溶液:(a)海水; (b)将200 mg.L-1 NaOH溶液加入海水和(c)蒸馏水作为基准而获得的碱性溶液。为了分析填充柱测试,在进料-分批反应器中使用在柱测试中测试的相同吸收溶液进行低浓度(100-2000 ppmv)的SO2平衡吸收测试。在填充塔中进行的实验测试表明,对于低至500 ppm的SO2浓度,通过使用大约2.91 kg.kg(-1)的液气质量比,可以实现98%以上的吸收效率。在这种情况下,解决方案(a)和(b)之间几乎没有差异。对于最高的SO2浓度(即2000 ppmv),液气比为3.44 kg.kg(-1)时观察到的效率最高为85%。平衡和动态数据的建模在Aspen Plus(R)V 8.6中进行。但是,尽管建模可确保很好地预测平衡数据,但它不能正确描述动态测试结果,而系统地低估了去除效率高于85%的测试。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号