化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
9期
3340-3349
,共10页
刘作华%孙瑞祥%王运东%陶长元%刘仁龙
劉作華%孫瑞祥%王運東%陶長元%劉仁龍
류작화%손서상%왕운동%도장원%류인룡
混合%混沌%搅拌槽%刚-柔组合搅拌桨%分形维数%CFD模拟%吸引子
混閤%混沌%攪拌槽%剛-柔組閤攪拌槳%分形維數%CFD模擬%吸引子
혼합%혼돈%교반조%강-유조합교반장%분형유수%CFD모의%흡인자
mixing%chaos%stirred vessel%rigid-flexible coupling impeller%fractal dimension%CFD simulation%attractor
合理设计搅拌反应器的桨叶,强化流体流动与混合行为,是实现流体高效、节能混合的重要手段。柔性体与刚性体组合,可设计出具有多体运动行为的刚-柔组合搅拌桨。结合PIV流场观测和CFD模拟,对比分析了刚性桨和刚-柔组合桨对流场结构及流体混沌混合行为的影响。结果表明,与刚性搅拌桨相比,刚-柔组合桨的柔性端强化能量传递,流体流速衰减速率降低25%,有利于搅拌桨输入能量在流场结构内的有效分配。传统刚性六凹叶和六直叶涡轮桨搅拌反应器内流体形成的流线结构具有明显的周期吸引子,其时均流场的分形维数分别为1.9046和1.9138。刚-柔组合六直叶涡轮桨搅拌反应器内流体流线呈明显的准周期性吸引子性质,其流场分形维数为1.9337,而刚-柔组合六凹叶涡轮桨搅拌反应器内流体流线具有典型的混沌吸引子性质,其流场分形维数为1.9545。刚-柔组合搅拌桨可改变流体流线的吸引子来调控流场的多尺度结构,强化流体混沌混合,实现高效节能操作。
閤理設計攪拌反應器的槳葉,彊化流體流動與混閤行為,是實現流體高效、節能混閤的重要手段。柔性體與剛性體組閤,可設計齣具有多體運動行為的剛-柔組閤攪拌槳。結閤PIV流場觀測和CFD模擬,對比分析瞭剛性槳和剛-柔組閤槳對流場結構及流體混沌混閤行為的影響。結果錶明,與剛性攪拌槳相比,剛-柔組閤槳的柔性耑彊化能量傳遞,流體流速衰減速率降低25%,有利于攪拌槳輸入能量在流場結構內的有效分配。傳統剛性六凹葉和六直葉渦輪槳攪拌反應器內流體形成的流線結構具有明顯的週期吸引子,其時均流場的分形維數分彆為1.9046和1.9138。剛-柔組閤六直葉渦輪槳攪拌反應器內流體流線呈明顯的準週期性吸引子性質,其流場分形維數為1.9337,而剛-柔組閤六凹葉渦輪槳攪拌反應器內流體流線具有典型的混沌吸引子性質,其流場分形維數為1.9545。剛-柔組閤攪拌槳可改變流體流線的吸引子來調控流場的多呎度結構,彊化流體混沌混閤,實現高效節能操作。
합리설계교반반응기적장협,강화류체류동여혼합행위,시실현류체고효、절능혼합적중요수단。유성체여강성체조합,가설계출구유다체운동행위적강-유조합교반장。결합PIV류장관측화CFD모의,대비분석료강성장화강-유조합장대류장결구급류체혼돈혼합행위적영향。결과표명,여강성교반장상비,강-유조합장적유성단강화능량전체,류체류속쇠감속솔강저25%,유리우교반장수입능량재류장결구내적유효분배。전통강성륙요협화륙직협와륜장교반반응기내류체형성적류선결구구유명현적주기흡인자,기시균류장적분형유수분별위1.9046화1.9138。강-유조합륙직협와륜장교반반응기내류체류선정명현적준주기성흡인자성질,기류장분형유수위1.9337,이강-유조합륙요협와륜장교반반응기내류체류선구유전형적혼돈흡인자성질,기류장분형유수위1.9545。강-유조합교반장가개변류체류선적흡인자래조공류장적다척도결구,강화류체혼돈혼합,실현고효절능조작。
Rational design of impellers in stirred vessels for strengthening the fluid flow and mixing is an important way to achieve efficient and energy-saving mixing. Rigid-flexible coupling impeller can be designed by combination of flexible body and rigid body, possessing multiple-body motion behavior. In this study, CFD simulation and PIV flow visualization were comparatively employed to analyze the difference between rigid impeller and rigid-flexible coupling impeller for fluid flow structure and mixing performance. Results showed that, compared with rigid impeller system, velocity decaying rate was reduced by 25% with rigid-flexible coupling impeller system, because it had the ability to intensify the input energy transportation by flexible part and distribute the input energy in flow field structure effectively. The streamline of the fluid stirred by rigid PBT-6 impeller and rigid RDT-6 impeller had obviously periodic attractor with fractal dimension 1.9046 and 1.9138 respectively. Rigid-flexible coupling impellers could intensify chaotic mixing of fluid and regulate the fractal dimension of flow field structure. The streamline of fluid stirred by flexible RDT-6 impeller had quasi-periodic attractors with fractal dimension of 1.9337, while the fractal dimension of chaotic attractor was 1.9545 with flexible PBT-6 impeller. It suggests that the flexible impeller could regulate multi-scale structure of the flow field by changing streamline attractor to intensify the chaotic mixing and achieve energy efficient operation.