化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2010年
3期
430-435
,共6页
雷建奇%祝贺%陈剑佩%吴高杰
雷建奇%祝賀%陳劍珮%吳高傑
뢰건기%축하%진검패%오고걸
翼型轴流桨%推力系数%计算流体力学%轴向速度%功率准数
翼型軸流槳%推力繫數%計算流體力學%軸嚮速度%功率準數
익형축류장%추력계수%계산류체역학%축향속도%공솔준수
hydrofoil impellers%thrust coefficient%CFD (computational fluid dynamics)%axial velocity%power number
对几种不同型式轴流桨的推力系数进行了实验及CFD模拟研究.结果表明:四宽叶翼型桨A的推力系数最大,三窄叶翼型桨D推力系数最小;模拟结果与实验结果有很好的吻合;四宽叶翼型桨A较其它几种轴流桨形成的全釜大循环更为彻底,没有发生分区现象;四宽叶翼型桨A在叶端线上的最大轴向速度远大于其它4种桨;四宽叶翼型桨A最大轴向速度随着r/R的增大而逐渐减小且逐渐向釜底方向移动.在水体系中的实验结果表明:当通气量Q_g为1.1 vvm,P/V≥1.5 kW/m~3时,四宽叶翼型桨A-透平桨组合的传质系数较双层透平桨组合高约9.6%.
對幾種不同型式軸流槳的推力繫數進行瞭實驗及CFD模擬研究.結果錶明:四寬葉翼型槳A的推力繫數最大,三窄葉翼型槳D推力繫數最小;模擬結果與實驗結果有很好的吻閤;四寬葉翼型槳A較其它幾種軸流槳形成的全釜大循環更為徹底,沒有髮生分區現象;四寬葉翼型槳A在葉耑線上的最大軸嚮速度遠大于其它4種槳;四寬葉翼型槳A最大軸嚮速度隨著r/R的增大而逐漸減小且逐漸嚮釜底方嚮移動.在水體繫中的實驗結果錶明:噹通氣量Q_g為1.1 vvm,P/V≥1.5 kW/m~3時,四寬葉翼型槳A-透平槳組閤的傳質繫數較雙層透平槳組閤高約9.6%.
대궤충불동형식축류장적추력계수진행료실험급CFD모의연구.결과표명:사관협익형장A적추력계수최대,삼착협익형장D추력계수최소;모의결과여실험결과유흔호적문합;사관협익형장A교기타궤충축류장형성적전부대순배경위철저,몰유발생분구현상;사관협익형장A재협단선상적최대축향속도원대우기타4충장;사관협익형장A최대축향속도수착r/R적증대이축점감소차축점향부저방향이동.재수체계중적실험결과표명:당통기량Q_g위1.1 vvm,P/V≥1.5 kW/m~3시,사관협익형장A-투평장조합적전질계수교쌍층투평장조합고약9.6%.
The thrust coefficient of different hydrofoil impellers was experimentally studied and simulated with CFD.Results showed that the thrust coefficient of four-broad-blade hydrofoil A is the largest,and that of three-narrow-blade hydrofoil D is the smallest.The simulation results axe in good agreement with experiment.Compared with other axial impellers,four-broad-blade hydrofoil A produces a fully developed circulation.The maximum axial velocity of four-broad-blade hydrofoil A is the biggest in these impellers at the vertical line of blade tip.The maximum axial velocity of four-broad-blade hydrofoil A gradually declines with the increase of r/R,and moves toward the bottom of the tank.Experimental results in water system indicated that the mass transfer coefficient (k_Lα) of four-broad-blade hydrofoil A-Rushton turbine (HF-A-RT) is 9.6% higher than that of Rushton turbine-Rushton turbine (RT-RT) when gas aerated rate is 1.1 vvm and the power consumption per volume (P/V) is not less than 1.5 kW/m~3.