山东化工
山東化工
산동화공
Shandong Chemical Industry
2015年
22期
38-41,44
,共5页
黄兆亮%王伯良%林秋汉%陈晓茹
黃兆亮%王伯良%林鞦漢%陳曉茹
황조량%왕백량%림추한%진효여
雾化%数值模拟%泰勒锥%FLUENT%电场
霧化%數值模擬%泰勒錐%FLUENT%電場
무화%수치모의%태륵추%FLUENT%전장
atomization%numerical simulation%taylor cone%FLUENT%electric field
利用 FLUENT 软件,对雾化器腔室内部流场进行模拟计算,研究了同轴气体流速对气体流型的影响,得到了该结构下流场的稳定域。在这种稳定域条件下,对液体输运特征进行计算。模拟电压对泰勒锥演变的影响和电压、液体表面张力、液体粘性对液滴二次破碎的影响。结果表明,电场强度改变,泰勒锥的形状会发生改变。电压为2000V、3000V、5000V 条件下,在一定范围内提高电场强度可以明显减小液滴平均粒径。在2000V 电压下,降低液体的表面张力可以显著降低液滴平均粒径;液体粘性对形成的液体平均粒径没有太大影响。
利用 FLUENT 軟件,對霧化器腔室內部流場進行模擬計算,研究瞭同軸氣體流速對氣體流型的影響,得到瞭該結構下流場的穩定域。在這種穩定域條件下,對液體輸運特徵進行計算。模擬電壓對泰勒錐縯變的影響和電壓、液體錶麵張力、液體粘性對液滴二次破碎的影響。結果錶明,電場彊度改變,泰勒錐的形狀會髮生改變。電壓為2000V、3000V、5000V 條件下,在一定範圍內提高電場彊度可以明顯減小液滴平均粒徑。在2000V 電壓下,降低液體的錶麵張力可以顯著降低液滴平均粒徑;液體粘性對形成的液體平均粒徑沒有太大影響。
이용 FLUENT 연건,대무화기강실내부류장진행모의계산,연구료동축기체류속대기체류형적영향,득도료해결구하류장적은정역。재저충은정역조건하,대액체수운특정진행계산。모의전압대태륵추연변적영향화전압、액체표면장력、액체점성대액적이차파쇄적영향。결과표명,전장강도개변,태륵추적형상회발생개변。전압위2000V、3000V、5000V 조건하,재일정범위내제고전장강도가이명현감소액적평균립경。재2000V 전압하,강저액체적표면장력가이현저강저액적평균립경;액체점성대형성적액체평균립경몰유태대영향。
FLUENT software was used to simulate the flow field inside the nebulizer chamber .The effects of gas velocity coaxial on gas flow pattern were studied .We got a steady flow field region of the structure .Under the stable region conditions, the liquid transport characteristics were simulated .The influence of voltage on the evolution of the Taylor cone and the influence of voltage, surface tension, viscosity on the droplets were simulated.The results showed that when the electric field intensity changed, the shape Taylor cone would change .It was found that, at 2000v, 3000v, 5000v, improving the electric field intensity could significantly reduce the average particle diameter of the droplets within a certain range.The average particle size was significantly reduced by reducing the surface tension of the liquid droplets at 2000v. Furthermore, the viscosity of liquid had little impact on the average particle diameter .