Experiment and simulation on the pyrite removal from the recirculating load of pulverizer with a dilute phase gas-solid fluidized bed  被引量:6

Experiment and simulation on the pyrite removal from the recirculating load of pulverizer with a dilute phase gas–solid fluidized bed

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作  者:Wang Shuai He Yaqun He Jingfeng Ge Linhan Liu Qing 

机构地区:[1]School of Chemical Engineering and Technology, China University of Mining & Technology

出  处:《International Journal of Mining Science and Technology》2013年第2期302-306,共5页矿业科学技术学报(英文版)

基  金:supported financially by the National Natural Science Foundation of China (Nos. 51074156 and 50921002)

摘  要:In order to reduce the energy consumption and subsequent air pollution of coal-fired power station, based on the analysis to size and density distribution of particles from the recirculating load of the classifier of pulverizer, the separation experiment on sampling material from power plant with a dilute phase fluidized bed to remove pyrite and other minerals and numerical simulation on the separation process were done. The results show that the minimum fluidization velocity is 1.62 cm/s. Pyrite and other minerals in the material are separated. Ash of the upper and bottom layer material account for 33.34% and 73.42% respectively and sulfur content occupy 1.12% and 8.96% respectively. Scanning electron microscopy and spectroscopy tests show that sulfur in the bottom material exist in the form of pyrite. Numerical simulation on the flow field form of the dilute phase separation bed with gas-solid two phase and particle motion verifies the experimental results.In order to reduce the energy consumption and subsequent air pollution of coal-fired power station, based on the analysis to size and density distribution of particles from the recirculating load of the classifier of pulverizer, the separation experiment on sampling material from power plant with a dilute phase fluidized bed to remove pyrite and other minerals and numerical simulation on the separation process were done. The results show that the minimum fluidization velocity is 1.62 cm/s. Pyrite and other minerals in the material are separated. Ash of the upper and bottom layer material account for 33.34% and 73.42% respectively and sulfur content occupy 1.12% and 8.96% respectively. Scanning electron microscopy and spectroscopy tests show that sulfur in the bottom material exist in the form of pyrite. Numerical simulation on the flow field form of the dilute phase separation bed with gas-solid two phase and particle motion verifies the experimental results.

关 键 词:Pulverizer Recirculating load of classifier Dilute phase fluidized bed Pyrite Numerical simulation 

分 类 号:TD951[矿业工程—选矿]

 

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