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Study On The Local Pressure Drop Characteristics Of Gas-liquid Two-phase Flow In A Combined Bend Under The Effect Of Gravity

Posted on:2024-01-14Degree:MasterType:Thesis
Country:ChinaCandidate:B WangFull Text:PDF
GTID:2542307115979789Subject:Applied Mechanics and Engineering Structure
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In the context of implementing energy conservation and emission reduction in the engineering practice,it is of apparent engineering guidance and academic value to research the local pressure drop characteristics of gas-liquid two-phase flows in combined bends under the effect of gravity.Because there is relatively less research on the local pressure drop characteristics of gas-liquid two-phase flows in the bends(especially the combined bends more suitable for the actual engineering practice)under the effect of gravity.In the current thesis,we use the Realizable k-εturbulence model combined with the Mixture two-phase flow model of the Fluent to systematically investigate the local pressure drop characteristics(mainly including the local pressure drop ratioλand the local pressure drop coefficientξ)of the gas-liquid two-phase flow in a single bend(namely,L-shaped bend)and a combined bend(namely,Z-shaped,90°,and 180°combined bend)under the effect of gravity.Specifically,the influence law of the local pressure drop ratioλand the local pressure drop coefficientξbetween the dimensional parameters,e.g.,the three different flow directions,the bend-diameter ratio R/D,the high-diameter ratio H/D,the gas-phase volume ratioα,and the liquid-phase Reynolds number Re_l(which is dimensionless by the gas-liquid two-phase flow velocity)are systematically investigated.First,the local pressure drop characteristics of the gas-liquid two-phase flow in the L-shaped bend under the effect of gravity are systematically studied in the parameters of R/D=1~7、α=0~0.3,and Re_l=2.9×10~4~2.1×10~5.The results show thatλincreases and then decreases with increasingαwhen R/D<2,andλshows the opposite trend when R/D>2;λincreases with increasing Re_l when 0.05≤α≤0.3,and the growth trend ofλ-Re_lrelationship curve remains almost constant when R/D>4;when 0.05≤α≤0.3,ξincreases continuously with the increase ofα,and the increasing trend gradually decreases;ξchanges more significantly whenαincreases from 0to 0.2,and after that it can be approximated that the change ofξis independent ofα;ξdecreases first with the increase of R/D and then tends to be stable.Secondly,the local pressure drop characteristics of the gas-liquid two-phase flow in the Z-bend under the effect of gravity are systematically studied in the parameters of R/D=1~8,H/D=1~16,α=0~0.3,and Re_l=2.9×10~4~2.1×10~5 in combination with three flow directions.The results show that keeping R/D=2 constant,λdecreases whenαincreases;λincreases with Re_l under different flow direction conditions,and the increase inλremains basically constant with the increase in H/D;when Re_l is relatively small,ξdecreases with the increase in Re_l,and as Re_l continues to increase,ξwill not change significantly with the change in Re_l;for upward flow,ξincreases with the increase of H/D,and for horizontal flow and downward flow,ξdecreases with the increase of H/D;ξdecreases first with the increase of R/D and then remains basically the same.Finally,three combination bends of 0°(Z-shaped),90°,and 180°are selected to investigate the intrinsic correlation between the adjacent influence effects(including the adjacent influence coefficient C and the adjacent influence length H_m)and H/D.Subsequently,the prediction equations for theξof the L-shaped and the three combinations bends with R/D,H/D,α,and Re_l are established based on many numerical results in both upward and downward flow directions.The results show that C shows the same trend with the change of H/D;C is 0°bend>90°bend>180°bend for upward flow,and 90°bend>0°bend>180°bend for downward flow;Hm shows the opposite variation law with C under the two flow conditions;the fitting error between the prediction equations and the numerical results is basically within 20%.
Keywords/Search Tags:gas?liquid two-phase flow, radius-diameter ratio, height-diameter ratio, Reynolds number, local pressure drop ratio, local resistance coefficient, adjacent influence effect
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