化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2010年
1期
89-93
,共5页
倪建军%梁钦锋%于广锁%于遵宏
倪建軍%樑欽鋒%于廣鎖%于遵宏
예건군%량흠봉%우엄쇄%우준굉
整体煤气化联合循环%气化炉%熔渣颗粒%辐射废锅%辐射传热
整體煤氣化聯閤循環%氣化爐%鎔渣顆粒%輻射廢鍋%輻射傳熱
정체매기화연합순배%기화로%용사과립%복사폐과%복사전열
IGCC%gasifier%molten-slag particle%radiant syngas cooler%radiative heat transfer
建立了多相流动和传热耦合数学模型,以实验室规模气化装置对模型进行了验证,发现计算值与实验值吻合较好.再通过该模型对气化炉与辐射废锅的接口进行了数值模拟,结果发现:气化炉底部锥体壁面有大量灰渣颗粒积聚,并在锥体上形成热阻较大的熔渣流;废锅拱顶存在长约4 m的回流区,部分颗粒被卷吸回流;此外,增加直段高度、加长冷却管和降低耐火砖厚度都将使接口工作温度下降;提高气化温度和操作负荷则会使接口工作温度上升,且气流流速也将随产气量的增加而提高.
建立瞭多相流動和傳熱耦閤數學模型,以實驗室規模氣化裝置對模型進行瞭驗證,髮現計算值與實驗值吻閤較好.再通過該模型對氣化爐與輻射廢鍋的接口進行瞭數值模擬,結果髮現:氣化爐底部錐體壁麵有大量灰渣顆粒積聚,併在錐體上形成熱阻較大的鎔渣流;廢鍋拱頂存在長約4 m的迴流區,部分顆粒被捲吸迴流;此外,增加直段高度、加長冷卻管和降低耐火磚厚度都將使接口工作溫度下降;提高氣化溫度和操作負荷則會使接口工作溫度上升,且氣流流速也將隨產氣量的增加而提高.
건립료다상류동화전열우합수학모형,이실험실규모기화장치대모형진행료험증,발현계산치여실험치문합교호.재통과해모형대기화로여복사폐과적접구진행료수치모의,결과발현:기화로저부추체벽면유대량회사과립적취,병재추체상형성열조교대적용사류;폐과공정존재장약4 m적회류구,부분과립피권흡회류;차외,증가직단고도、가장냉각관화강저내화전후도도장사접구공작온도하강;제고기화온도화조작부하칙회사접구공작온도상승,차기류류속야장수산기량적증가이제고.
A novel model of multiphase flow and radiative heat transfer combination was established. The results predicted are in good agreement with the lab-scale gasifier experimental data. And this model was used to carry out the unsteady calculation about the connection of entrained flow gasifier to the syngas cooler. It shows that a large number of particles deposite on the cone of the bottom of gasifier and form the slag flow with larger thermal resistance. The vault of radiant syngas cooler (RSC) has a reflux region of 4 m in length and many slag particles are entrained back. Moreover, the temperature of the connection decreases with increasing the straight section of connection and the height of cooling tube and decreasing the thickness of firebrick. The temperature of the connection increases with increasing the gasification operation temperature and the operation load. The velocity of gas flow also increases with the increasing of the syngas production capacity.