化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
3期
965-971
,共7页
张向宇%郑树%周怀春%徐宏杰
張嚮宇%鄭樹%週懷春%徐宏傑
장향우%정수%주부춘%서굉걸
管式炉%辐射%炉管%建模%热通量
管式爐%輻射%爐管%建模%熱通量
관식로%복사%로관%건모%열통량
tubular furnace%radiation%pipe%modeling%heat flux
准确在线检测管壁表面分布式温度是优化管式炉加热工艺的关键所在。以一台工业管式裂解炉为试验对象,结合辐射图像处理方法,开展了管式炉炉管表面温度可视化检测研究。采用基于Monte Carlo的DRESOR法求解具有复杂边界条件的管式炉辐射成像模型,实现了炉管辐射与火焰辐射、炉壁辐射的解耦计算,对炉管表面温度与热通量分布进行了在线监测,并研究了二者随工质流动方向的变化趋势。经过验证,温度测量误差小于2%,测量误差主要出现在最高和最低温区域。该项研究将有助于指导管式炉燃烧调整,改进加热工艺,提高炉管表面受热均匀性,延长炉管工作寿命。
準確在線檢測管壁錶麵分佈式溫度是優化管式爐加熱工藝的關鍵所在。以一檯工業管式裂解爐為試驗對象,結閤輻射圖像處理方法,開展瞭管式爐爐管錶麵溫度可視化檢測研究。採用基于Monte Carlo的DRESOR法求解具有複雜邊界條件的管式爐輻射成像模型,實現瞭爐管輻射與火燄輻射、爐壁輻射的解耦計算,對爐管錶麵溫度與熱通量分佈進行瞭在線鑑測,併研究瞭二者隨工質流動方嚮的變化趨勢。經過驗證,溫度測量誤差小于2%,測量誤差主要齣現在最高和最低溫區域。該項研究將有助于指導管式爐燃燒調整,改進加熱工藝,提高爐管錶麵受熱均勻性,延長爐管工作壽命。
준학재선검측관벽표면분포식온도시우화관식로가열공예적관건소재。이일태공업관식렬해로위시험대상,결합복사도상처리방법,개전료관식로로관표면온도가시화검측연구。채용기우Monte Carlo적DRESOR법구해구유복잡변계조건적관식로복사성상모형,실현료로관복사여화염복사、로벽복사적해우계산,대로관표면온도여열통량분포진행료재선감측,병연구료이자수공질류동방향적변화추세。경과험증,온도측량오차소우2%,측량오차주요출현재최고화최저온구역。해항연구장유조우지도관식로연소조정,개진가열공예,제고로관표면수열균균성,연장로관공작수명。
Accurate measurement of temperature distribution of pipe surface becomes the key issue for optimization of heating process in tubular furnace. Experiment research of visualization of pipe temperature distribution was conducted on an industrial ethylene cracking furnace based on radiation image processing. Inside the furnace pipe, thermal cracking reaction of naphtha occurs, whose reaction heat is provided by eight burners located on the bottom, and the fuel is natural gas. Coking of furnace pipe was ignored in the model. In order to deal with the radiative heat transfer equation with complex boundary condition in the tubular furnace, a DRESOR method based on Monte Carlo principle was used, and the radiations from tubes, flame and furnace wall were decoupled. Sixteen CCD cameras were mounted on the furnace wall in order to capture the flame image which was transferred into boundary radiation intensity distribution by blackbody calibration. A revised Tikhonov regularization method was used to solve the morbid radiation image equation, and the distributions of pipe temperature and heat flux were measured online and their variation trends with flow direction of naphtha were also discussed. Validated by two different methods, temperature reconstruction error was less than 2%and maximum deviation was within 20K, and the major error occurred on the maximum and minimum temperature areas. This study would be useful for adjustment of combustion and heating process in tubular furnace, and would improve the uniformity of pipe surface temperature in order to extend their working life.