化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2014年
6期
48-53,68
,共7页
赵传伟%李增亮%许文艺%吴海燕
趙傳偉%李增亮%許文藝%吳海燕
조전위%리증량%허문예%오해연
水力旋流器%结构参数%大涡模拟%正交试验设计%优化
水力鏇流器%結構參數%大渦模擬%正交試驗設計%優化
수력선류기%결구삼수%대와모의%정교시험설계%우화
hydrocyclone%structural parameter%large eddy simulation%orthogonal experimental design%optimization
基于正交试验设计,以底流含油质量浓度低为优化目标,将欧拉-欧拉法与大涡模拟(LES)相结合,优化其主要结构参数并与试验结果进行对比。结果表明,总分流比为0.3,0.4,0.5,0.6时,数值模拟预测的优化后底流含油质量浓度较优化前分别平均减小14.4%,13.1%,15.1%,15.7%,与试验结果(13.6%,11.6%,13.8%,13.0%)相比,误差均小于5%;总分流比为0.3-0.6时,随着入口流量的增大,底流含油质量浓度先减小后增大;入口流量为75-215 m3/d时,随着总分流比的增大,底流含油质量浓度先减小后增大。入口流量为118-183 m3/d且总分流比为0.3-0.7时,优化后的双级串联式水力旋流器的底流含油质量浓度不大于200 mg/L。试验验证了数值模拟的可靠性。
基于正交試驗設計,以底流含油質量濃度低為優化目標,將歐拉-歐拉法與大渦模擬(LES)相結閤,優化其主要結構參數併與試驗結果進行對比。結果錶明,總分流比為0.3,0.4,0.5,0.6時,數值模擬預測的優化後底流含油質量濃度較優化前分彆平均減小14.4%,13.1%,15.1%,15.7%,與試驗結果(13.6%,11.6%,13.8%,13.0%)相比,誤差均小于5%;總分流比為0.3-0.6時,隨著入口流量的增大,底流含油質量濃度先減小後增大;入口流量為75-215 m3/d時,隨著總分流比的增大,底流含油質量濃度先減小後增大。入口流量為118-183 m3/d且總分流比為0.3-0.7時,優化後的雙級串聯式水力鏇流器的底流含油質量濃度不大于200 mg/L。試驗驗證瞭數值模擬的可靠性。
기우정교시험설계,이저류함유질량농도저위우화목표,장구랍-구랍법여대와모의(LES)상결합,우화기주요결구삼수병여시험결과진행대비。결과표명,총분류비위0.3,0.4,0.5,0.6시,수치모의예측적우화후저류함유질량농도교우화전분별평균감소14.4%,13.1%,15.1%,15.7%,여시험결과(13.6%,11.6%,13.8%,13.0%)상비,오차균소우5%;총분류비위0.3-0.6시,수착입구류량적증대,저류함유질량농도선감소후증대;입구류량위75-215 m3/d시,수착총분류비적증대,저류함유질량농도선감소후증대。입구류량위118-183 m3/d차총분류비위0.3-0.7시,우화후적쌍급천련식수력선류기적저류함유질량농도불대우200 mg/L。시험험증료수치모의적가고성。
Based on orthogonal experimental design and with lower oil mass concentration of underflow as optimal objective,the Euler-Euler approach and large eddy simulation (LES ) were combined and adopted in this simulation to systematically optimize the structural parameters of the downhole dual-stage tandem hydrocyclone,and the predictions were compared with experimental results.The results show that when the total split ratio is 0.3, 0.4,0.5,0.6,the underflow′s oil mass concentration of the optimized hydrocyclone is reduced by 1 4.4%, 1 3.1%,1 5.1%,1 5.7%respectively on average compared with that without optimization,and the errors between simulation and the experimental results (1 3 .6%,1 1 .6%,1 3 .8% ,1 3 .0%)are not more than 5%.When the total spit ratio is 0.3-0.6,the oil mass concentration of the underflow decreases firstly and then increases with the increasing inlet flow rate.When the inlet flow rate is 75-21 5 m3/d,the oil mass concentration of underflow decreases firstly and then increases with the increasing total spit ratio.After optimization,when the inlet flow rate is 1 1 8-1 83 m3/d and the total split ratio is 0.3-0.7,the oil mass concentration of underflow is not more than 200 mg/L. The reliability of numerical simulation is verified by experiment.