中国电机工程学报
中國電機工程學報
중국전궤공정학보
ZHONGGUO DIANJI GONGCHENG XUEBAO
2013年
26期
8-13
,共6页
王虎%李少华%刘大任%马文娥%张庆喆
王虎%李少華%劉大任%馬文娥%張慶喆
왕호%리소화%류대임%마문아%장경철
循环流化床%双膜理论%传质模型%Matlab%脱硫效率
循環流化床%雙膜理論%傳質模型%Matlab%脫硫效率
순배류화상%쌍막이론%전질모형%Matlab%탈류효솔
circulating fluidized bed%two-film theory%mass transfer model%Matlab%desulfurization efficiency
为揭示循环流化床烟气脱硫反应的机制,探寻重要参数对脱硫效率的影响情况,建立考虑脱硫剂浆滴内化学吸收过程的传质模型。该模型以双膜理论作为建模基础。在建立模型过程中,不仅考虑了塔内反应过程,而且考虑了外循环物料对脱硫效率的影响。将模型嵌入 Matlab 软件中进行数值计算,分析增湿水量和钙硫比对脱硫效率的影响情况。通过计算值与某电厂循环流化床脱硫系统运行数据的比对,发现该计算值与实测值的拟合度较高。模型的误差不大于5.1%,比较其他的模型具有较高的精度。该模型可用于优化运行参数,并在电厂脱硫系统变工况运行时预测脱硫效率。
為揭示循環流化床煙氣脫硫反應的機製,探尋重要參數對脫硫效率的影響情況,建立攷慮脫硫劑漿滴內化學吸收過程的傳質模型。該模型以雙膜理論作為建模基礎。在建立模型過程中,不僅攷慮瞭塔內反應過程,而且攷慮瞭外循環物料對脫硫效率的影響。將模型嵌入 Matlab 軟件中進行數值計算,分析增濕水量和鈣硫比對脫硫效率的影響情況。通過計算值與某電廠循環流化床脫硫繫統運行數據的比對,髮現該計算值與實測值的擬閤度較高。模型的誤差不大于5.1%,比較其他的模型具有較高的精度。該模型可用于優化運行參數,併在電廠脫硫繫統變工況運行時預測脫硫效率。
위게시순배류화상연기탈류반응적궤제,탐심중요삼수대탈류효솔적영향정황,건립고필탈류제장적내화학흡수과정적전질모형。해모형이쌍막이론작위건모기출。재건립모형과정중,불부고필료탑내반응과정,이차고필료외순배물료대탈류효솔적영향。장모형감입 Matlab 연건중진행수치계산,분석증습수량화개류비대탈류효솔적영향정황。통과계산치여모전엄순배류화상탈류계통운행수거적비대,발현해계산치여실측치적의합도교고。모형적오차불대우5.1%,비교기타적모형구유교고적정도。해모형가용우우화운행삼수,병재전엄탈류계통변공황운행시예측탈류효솔。
To reveal the reaction mechanism of flue gas desulfurization in a circulating fluidized-bed boiler and investigate the influence of some important parameters on the efficiency of desulfurization, a mass transfer model was established with the chemical absorption process inside the desulfurizing slurry drops being taken into account. The model was based on the two-film theory. During establishment of the model, both the influence of reaction process inside the tower and that of externally circulating material on desulfurization efficiency were both considered in the model. The model was embedded in the software of Matlab to carry out numerical calculation, by which the effects of humidifying water amount and calcium/sulfur ratio on desulfurization efficiency were analyzed. Compared with the operating data of a CFB desulfurization system, the calculated results were found agreed well with the measured values.The model has a higher accuracy than other models with a max error of 5.1%. The model can be used to optimize operating parameters and to predict desulfurization efficiency when a desulfurization system operates under varied conditions.