原子能科学技术
原子能科學技術
원자능과학기술
ATOMIC ENERGY SCIENCE AND TECHNOLOGY
2014年
1期
33-38
,共6页
王洋%阎昌琪%孙立成%金光远%闫超星
王洋%閻昌琪%孫立成%金光遠%閆超星
왕양%염창기%손립성%금광원%염초성
窄矩形通道%弹状流%液膜
窄矩形通道%彈狀流%液膜
착구형통도%탄상류%액막
narrow rectangular channel%slug flow%liquid film
气液两相弹状流广泛存在于工程领域,弹状流中液膜特性对弹状流模型的建立具有重要意义。为此利用高速摄像系统,对竖直窄矩形通道(3.25 mm ×40 mm )内弹状流中液膜进行了可视化研究。实验中发现窄矩形通道中气弹左右两侧窄边液膜厚度不等且存在波动,但其对两侧液膜速度影响较小,两侧液膜速度相等。液膜脱离厚度主要受两相流速及气弹长度影响。液膜脱离速度随液相折算速度增加而增大;在低液相流速时,随气相折算速度增加而减小;当液相流速≥1.204 m/s时,液膜不下落,液膜脱离速度随气相速度变化较小,主要受液相流速影响。
氣液兩相彈狀流廣汎存在于工程領域,彈狀流中液膜特性對彈狀流模型的建立具有重要意義。為此利用高速攝像繫統,對豎直窄矩形通道(3.25 mm ×40 mm )內彈狀流中液膜進行瞭可視化研究。實驗中髮現窄矩形通道中氣彈左右兩側窄邊液膜厚度不等且存在波動,但其對兩側液膜速度影響較小,兩側液膜速度相等。液膜脫離厚度主要受兩相流速及氣彈長度影響。液膜脫離速度隨液相摺算速度增加而增大;在低液相流速時,隨氣相摺算速度增加而減小;噹液相流速≥1.204 m/s時,液膜不下落,液膜脫離速度隨氣相速度變化較小,主要受液相流速影響。
기액량상탄상류엄범존재우공정영역,탄상류중액막특성대탄상류모형적건립구유중요의의。위차이용고속섭상계통,대수직착구형통도(3.25 mm ×40 mm )내탄상류중액막진행료가시화연구。실험중발현착구형통도중기탄좌우량측착변액막후도불등차존재파동,단기대량측액막속도영향교소,량측액막속도상등。액막탈리후도주요수량상류속급기탄장도영향。액막탈리속도수액상절산속도증가이증대;재저액상류속시,수기상절산속도증가이감소;당액상류속≥1.204 m/s시,액막불하락,액막탈리속도수기상속도변화교소,주요수액상류속영향。
Gas-liquid slug flow is widely encountered in many practical industrial applications . A detailed understanding of the hydrodynamics of the liquid film surrounding gas slug has important significance for modeling of the slug flow . Non-intrusive flow visualization using a high speed video camera system was applied to study liquid film characteristics of slug flow in a vertical narrow rectangular channel (3.25 mm × 40 mm) .The liquid film thicknesses on both left and right narrow sides surrounding gas slug are different and wavy ,but it has a weak effect on liquid film velocity and the velocities on two sides are equal .The gas and liquid velocity as well as the length of gas slug have a significant effect on the liquid film breaking away thickness .The liquid film breaking away velocity increases with liquid superficial velocity ,and decreases with the increase of gas superficial velocity at low liquid velocity .The film does not descend and the gas superficial velocity has no significant effect on liquid film breaking away velocity at high liquid velocity (jL ≥1.204 m/s) ,it is mainly determined by the liquid flow rate .