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- あつひろ そや
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1 1
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6 6 ( ) ( ) (Bubble Flow) (Slug Flow) Churn Flow (Annular Flow)
7 7 気泡流 スラグ流 チャーン流 環状流 小 気体の流量 大 Fig.1..1
8 8 Griffith -Wallis Griffith Wallis Frm Taitel-Dukler Taital Dukler 198 jg, jl Fig.1..1 X CT CT X CT X 5 X CT
9 mm PDF PSD Fig 小気泡流 1..1 気泡流 l E /D=5 1 5 環状流.1 スラグ流 スラグ, チャーン流 Fig.1..1 Taitel-Dukler 内径 :Φmm L/D:5.7 差圧測定区間距離 :11mm P(Δ (ΔP * a )..1 P(Δ (ΔP * a ).1.5 P(Δ (ΔP * a ).5... P(Δ (ΔP * a ) ΔP * a 1 ΔP * a 1 ΔP * a 1 ΔP * a 気泡流 スラグ流 チャーン流 環状流 差圧測定区間距離 :mm P(Δ (ΔP * a ).1.5 P(Δ (ΔP * a ).. 1 ΔP * a チャーン流 1 ΔP * a 環状流 Fig.1..
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12 mm 1mm
13 1 5.5P-9.5VA5/6.9 6L/min 17L SMA-,SMG-1.5L/min.5 5L/min 5 5L/min 5 5L/min 1 1 L5 OMEGA..L/min 5 1 Validyne DP15-6-N-1-S--A 8.8cm Validyne CD8- DR-M
14 1 (PHOTRON FASTCAM-Net Max) 5fps 8.7 PSR1V5W Top Tank AMP HVC Digital Recorder DPS..... VCR Pressure Gauge Thermo-Couple Flow Meter Mixing Room Drain Pipe Valve Drain Gravity Tank Bottom Tank Flow Meter Compressor Digital Multi Meter Thermo-Couple Filter Air Separator Fig..1
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17 L/min.5 1.5L/min 8 1 D D 1D Hz 1 Fig..1.1 Taitel-Dukler Table Annular Bubble J l.1 Slug Churn J g Fig..1.1 Taitel-Dukler
18 18 Table..1.1 番号 (No.) 空気みかけ速度 (cm/s) 水みかけ速度 (cm/s) 体積流量比
19 19 fig..1 fig..8 D Table i 1,,, i i+1 (6 )
20 (1) () () () Fig...1 (No.1 No.)
21 1 (5) (6) (7) (8) Fig... (No.8 No.5)
22 (9) (1) (11) (1) Fig... (No.9 No.1)
23 (1) (1) (15) (16) Fig... (No.1 No.16)
24 (17) (18) (19) () Fig...5 (No.17 No.)
25 5 (1) () () () Fig...6 (No.1 No.)
26 6 (5) (6) (7) (8) Fig...7 (No.5 No.8)
27 7 (9) () (1) () Fig...8 (No.9 No.)
28 8
29 9 X Y (X,Y) fig.1.1 No. (fig..6 No.) X Y L X Y LG X Y G X Y GL L LG G GL X =. 5 Y =. 5
30 気体スラグ 液体スラグ 液体スラグが通過 気体スラグが通過 液体スラグ 気体スラグ Fig.1.1
31 1 fig
32 (fig..8 ) ex.no.(fig..1) L fig..1 (.9,.9) ex.no.6(fig..) L y = x ex.no.15(fig..) y = x L G LG GL ex.no(fug..) y = x L G (,) Y 1 1 ( x = ) ( y = x ) ex.no6(fig..5) 1 y = x y = x x = L y = x ex.no9(fig..6) G ex.no(fig..7)
33 Y x=.5 y=x Y x=.5 y=x 1 y=.5 1 y= Fig..1 No. X X Fig.. No.6 Y x=.5 y=x Y x= x=.5 y=x y=.5 X Fig.. No y=.5 y= x/ X Fig.. No.
34 Y x= x=.5 y=x Y x= x=.5 y=x y=.5 y= x/ X Fig..5 No y=.5 y= x/ X Fig..6 No.9 Y x=.5 y=x y=.5 X Fig..7 No. Y 1 x=.5 GL L G LG Fig..8 y=.5 X
35 5 1 Fig.. Fig..5 Fig..6, y = x x = x = 1 y = x x = Fig..9 Fig..9 A B No No5 Taitel-Dukler Slug-Churn No6 A B x =
36 Y x= 6 A C y= x/ B X Fig..9 No5
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40 [1] (1981) 7- []Taital,Y., Bornea,D. and Dukler,A.E., Modelling Flow Pattern Transitions for Steady Upward Gas-Liquid Flow in Vertical Tubes, AIChE J, 6-, pp.5-5, 198 [] (1995) 5-5 [] ()
41 1
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卒業論文
1 2 3 A 4 6 ( ) (Bubble Flow) (Slug Flow) Churn Flow (Annular Flow) 7 Bubble Flow Slug Flow Churn Flow Annular Flow Fig.1.2.1 8 1961 Griffith Wallis..7 1 2.34 198 Taitel Dukler 1983 Fig.1.3.1. Taitel-Dukler
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