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作 者:黄雅琴 李彩亭[1,2] 李珊红[1,2] 张哲 黄乐 张智雄 HUANG Yaqin;LI Caiting;LI Shanhong;ZHANG Zhe;HUANG Le;ZHANG Zhixiong(College of Environmental Science and Engineering,H unan University,Changsha 410082,China;Key Laboratory of Environmental Biology and Pollution Control,Ministry of Education,Hunan University,Changsha 410082,China)
机构地区:[1]湖南大学环境科学与工程学院,长沙410082 [2]湖南大学,环境生物与控制教育部重点实验室,长沙410082
出 处:《环境工程学报》2020年第8期2222-2231,共10页Chinese Journal of Environmental Engineering
基 金:国家重点研发计划(2016YFC0204100);湖南省重点研发计划(2018SK2032,2018SK2033)。
摘 要:针对燃煤工业锅炉烟尘超低排放的要求,采用数值模拟方法,研究了旋风除尘器(A)和内部滤袋前无导流板(B)、有导流板(C)或开孔挡板(D)的几种旋风-布袋复合除尘器的流场。结果表明:除尘器C的流场较均匀,较高风速时压降低于除尘器B、D。进一步模拟了除尘器A、C的分级效率,发现对于粒径低于15μm的颗粒,除尘器A去除率低于60%,除尘器C去除率高于97.8%。且复合除尘器占地小,滤袋寿命长,具有广阔的应用前景。上述数值模拟结果可为复合除尘器的优化设计提供参考。For the ultra-low emission of flue gas and dust from coal-fired industrial boilers,a numerical simulation method was used to study the flow fields of cyclone dust collector(A)and several kinds of cyclonebag composite dust collectors without baffle(B),with baffle(C)or perforated baffle(D)in front of inner filter bag.The results showed that the flow field of cyclone-bag composite dust collector C was more uniform than others,and its pressure drop was lower than cyclone-bag composite dust collectors of B and D at a higher inlet velocity.The grading efficiencies of cyclone-bag composite dust collectors of A and C were further simulated,it was found that for particles smaller than 15 micrometers,the corresponding removal efficiency by cyclone-bag composite dust collector A was lower than 60%,while the corresponding removal efficiency by cyclone-bag composite dust collector C was higher than 97.8%.Moreover,with advantages of less space,lower filter bag load and longer cleaning cycle,the new composite dust collector has a broad application prospect.The results of above numerical simulation provide guidelines for the design and optimization of the composite dust collector.
分 类 号:X701.2[环境科学与工程—环境工程]
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