Effects of the Updated National Emission Regulation in China on

May 15, 2013 - However, the new National Emission Regulation (NER) issued in early 2012 ... Progress of circulating fluidized bed combustion technolog...
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The Effects of the Update National Emission Regulation in China on Circulating Fluidized Bed Boilers and the Solutions Jingji Li, Hairui Yang, Yuxin Wu, Junfu Lu, and Guangxi Yue Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/es4001888 • Publication Date (Web): 15 May 2013 Downloaded from http://pubs.acs.org on May 18, 2013

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Environmental Science & Technology

The Effects of the Update National Emission Regulation in China on Circulating Fluidized Bed Boilers and the Solutions Jingji Li, Hairui Yang, Yuxin Wu*, Junfu Lv, Guangxi Yue Key Laboratory for Thermal Science and Power Engineering of Ministry of Education Beijing Key Laboratory of CO2 Utilization and Reduction Technology Department of Thermal Engineering, Tsinghua University, Beijing 100084, China *Email: [email protected], Tel:86-10-62773384,Fax: 86-10-62773384

KEYWORDS: Update National Emission Regulation, China, CFB boiler, Effect, Solution ABSTRACT: The advantage of circulating fluidized bed (CFB) boiler in China is the utilization of low rank coal with low cost emission control. However, the new National Emission Regulation (NER) issued in early 2012 brings much more stringent challenges on the CFB industries, which also causes much attention from other countries. Based on the principle of a CFB boiler and the previous operating experiences, it is possible for the CFB boilers to meet the new NER and maintain the advantage in low cost emission control, while, more influences should be considered in the design and operation of a CFB boiler. In order to meet the requirement of the new NER, the fly ash collector should adopt the bag house or combination of electrostatic precipitator

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and bag filter to ensure the dust emission of less than 30mg⋅Nm-3. For the SO2 emission control, the bed temperature should be strictly lower than 900 oC to maintain high reactivity and pores. The limestone particle size distribution should be ranged within a special scope to optimize the residence time and gas-solid reaction. At the same time, the injecting point should be optimized to ensure fast contact of lime with oxygen. In such conditions, the desulphurization efficiency could be increased more than 90%. For lower sulphur content fuels (