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10:00$B!A(B 10:20 | R104 | $B3IYB1):,$K$h$jM65/$5$l$k@]F0$,AXN.:.9g$K5Z$\$91F6A(B
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| S-39 | 362 |
10:20$B!A(B 10:40 | R105 | $BA/L@$JN.L.@~2D;k2=
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$B66K\(B $B=SJe(B $B!&(B $B@>@n(B $BC#:H(B $B!&(B ($B@5(B)$B0f>e(B $B5AO/(B | Visualization Streakline Chaos Mixing
| S-39 | 76 |
10:40$B!A(B 11:00 | R106 | $BN.L.@~$rMxMQ$7$?%^%C%/%9%V%l%s%IMc$K$*$1$kN.$l$N2D;k2=(B
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| S-39 | 750 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B9b66(B $B9,;J(B) |
11:00$B!A(B 11:20 | R107 | $B9-$$%l%$%N%k%:?tHO0O$rBP>]$H$7$?(BHi-F$B%_%-%5!
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| S-39 | 596 |
11:20$B!A(B 11:40 | R108 | $B@55U8r8_2sE>Mc3IYB$K$*$1$kN.BNJQ7AFC@-(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@gED(B $BAa5*(B $B!&(B ($B@5(B)$B8VED(B $B1YG7(B $B!&(B ($B@5(B)$BNkLZ(B $BMN(B | mixing unsteady impeller
| S-39 | 173 |
11:40$B!A(B 12:00 | R109 | $BMpN.0h$K$*$1$kJ?%Q%I%kMcGXLLN.F0@)8fK!$H$=$NFC@-I>2A(B
($BJ!2,Bg9)(B) $B!{(B($B3X(B)$BN6(B $BGnK~(B $B!&(B ($B@5(B)$BNk@n(B $B0l8J(B | Turbulent mixing paddle type impeller power consumption
| S-39 | 393 |
|
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13:00$B!A(B 13:40 | R113 | [$BE8K>9V1i(B] $B:.$<$k2J3X(B
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| S-39 | 464 |
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $BBgB<(B $BD>?M(B) |
13:40$B!A(B 14:00 | R115 | $BO"B33IYBAe$rMQ$$$?:.9gA`:n$K$*$1$kG;EY2t%9%1!<%k$N8!F$(B
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| S-39 | 601 |
14:00$B!A(B 14:20 | R116 | $B>e2
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| S-39 | 618 |
14:20$B!A(B 14:40 | R117 | MPS$BK!$rMQ$$$?HsDj>o3IYB$N%7%_%e%l!<%7%g%s(B
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| S-39 | 456 |
(14:40$B!A(B15:40)$B!!(B($B:BD9(B $BLg3p(B $B=( |
14:40$B!A(B 15:00 | R118 | $B2=3XH?1~$rMxMQ$7$?:.9g;~4VB,Dj$NLdBjE@(B
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$B66K\(B $B=SJe(B $B!&(B $B@>B<(B $BN<=S(B $B!&(B ($B@5(B)$B0f>e(B $B5AO/(B | Fluid Mixing Mixing Time Chemical Reaction
| S-39 | 320 |
15:00$B!A(B 15:20 | R119 | [$BM%=(O@J8>^(B] $B3IYBAeFb$K$*$1$k8IN):.9gNN0h$NM}O@E*2r@O(B
($B:eBg4p9)(B) $B!{(B($B@5(B)$B0f>e(B $B5AO/(B $B!&(B ($B;00f2=3X(B) ($B@5(B)$B0KF#(B $B42G7(B $B!&(B ($B%@%$%-%s9)6H(B) ($B@5(B)$BCfED(B $BA6OB(B $B!&(B ($B:eBg4p9)(B) ($B@5(B)$B66K\(B $B=SJe(B | Isolated Mixing Region Synchronization Visualization
| S-39 | 66 |
15:20$B!A(B 15:40 | R120 | $B3IYBAeFb$N8IN):.9gNN0h$K5Z$\$929EYJQ2=$N8z2L(B
($B?@8MBg1!9)(B) $B!{(B($B@5(B)$BBgB<(B $BD>?M(B $B!&(B ($B?@8MBg9)(B) Shahirudin Nor Hanizah $B!&(B ($B?@8MBg1!9)(B) Alatengtuya $B!&(B ($B?@8MBg9)(B) $BEDCf(B $B5WEP(B $B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B7'C+(B $B595W(B $B!&(B ($B@5(B)$BKY9>(B $B9';K(B | isolated mixing region temperature change topological structure
| S-39 | 735 |
(15:40$B!A(B16:40)$B!!(B($B:BD9(B $B66K\(B $B=SJe(B) |
15:40$B!A(B 16:00 | R121 | $B5$1UJ,;6$,5Z$\$99bG4EY1U$N:.9g$X$N1F6A(B
($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B02Ln(B $B@i?R(B $B!&(B ($B@5(B)$B9bH*(B $BJ]G7(B $B!&(B ($B@5(B)$B9b66(B $B9,;J(B $B!&(B (DIC) $B4X:,(B $B6Q(B | Gas Dispersion Mixing Time Highly Viscous Liquids
| S-39 | 250 |
16:00$B!A(B 16:20 | R122 | $B79
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| S-39 | 390 |
16:20$B!A(B 16:40 | R123 | O$B!?(BW$B%(%^%k%7%g%s$rJ,;6Aj$KMxMQ$7$?9bG4EY!&1UE)J,NvB.EY$N7WB,K!(B
($B%+%M%+(B) $B!{(B($B@5(B)$B6bC+(B $B7rEP(B $B!&(B ($B@5(B)$B?@ED(B $B>45W(B $B!&(B ($B2#9qBg9)(B) ($B@5(B)$B>e%N;3(B $B<~(B $B!&(B ($B@5(B)$B?N;V(B $BOBI'(B $B!&(B ($B@5(B)$B;03Q(B $BN4B@(B | liquid-liquid dispersion measuring drop diameter drop breakage rate
| S-39 | 245 |
R$B2q>l(B $BBh(B2$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BARDE(B $B@5J8(B) |
9:00$B!A(B 9:20 | R201 | $B2sE>1_E{7?1U1UCj=PAuCV$K$*$1$kN.F0>uBV$K5Z$\$9A`:n>r7o$N1F6A(B
($B2#9qBg9)(B) $B!{(B($B3X(B)$BT"0f(B $B2BF`;R(B $B!&(B ($B@5(B)$B;03Q(B $BN4B@(B $B!&(B ($B@5(B)$B?N;V(B $BOBI'(B $B!&(B ($B@5(B)$B>e%N;3(B $B<~(B $B!&(B ($B86;RNO5!9=(B) $BJ?Ln(B $B909/(B $B!&(B $B2.Ln(B $B1Q $B!&(B $B:4Ln(B $BM:0l(B | mixing liquid-liquid extraction PIV
| S-39 | 643 |
9:20$B!A(B 9:40 | R202 | $BN.BN$NN.$lJ}8~$NG;EY%`%i$r8z2LE*$K6Q0l2=$G$-$k@E;_7?%_%-%5$N8!F$(B
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| S-39 | 70 |
9:40$B!A(B 10:00 | R203 | [$BM%=(O@J8>^(B] $B6~6J7?Hy>.%A%c%M%k$N:.9g@-G=Hf3S(B
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| S-39 | 113 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B?N;V(B $BOBI'(B) |
10:00$B!A(B 10:20 | R204 | $BH?1~>=@O$K$*$1$kN3;R7A>u$K5Z$\$9N.F0$N1F6A(B
($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B4d:j(B $BC#Li(B $B!&(B ($B@5(B)$B9bH*(B $BJ]G7(B $B!&(B ($B@5(B)$B9b66(B $B9,;J(B | Crystallization Process Particle Shape Mixing
| S-39 | 474 |
10:20$B!A(B 10:40 | R205 | $B%@%&%J!
($BElBg@88&(B) $B!{(B($B@5(B)$BIz8+(B $B@i?R(B $B!&(B ($B90Bg?7%(%M8&(B) ($B@5(B)$B41(B $B9q@6(B $B!&(B ($BElBg@88&(B) ($B3X(B)$BCfB<(B $BM-(B $B!&(B ($B@5(B)$B@PB+(B $B??E5(B $B!&(B ($B@5(B)$BDi(B $BFX;J(B $B!&(B ($B;:Am8&(B) ($B@5(B)$BNkLZ(B $BA1;0(B $B!&(B (Sinapore$B9qBg(B) Cheng Yongpan $B!&(B Wang Chi-Hwa | downer solid-solid mixing coal pyrolyzer
| S-39 | 179 |
10:40$B!A(B 11:00 | R206 | $BJ#9g:`NA$N:.9g>uBV$NDjNL2=(B: $BB?3,AX%9%1!<%k$NIT6Q0l@-(B
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| S-39 | 51 |
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11:00$B!A(B 11:20 | R207 | $BFs<4%9%/%j%e2!=P5!$N?75,:.N}%(%l%a%s%H(B:$B79 2A(B
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| S-39 | 57 |
11:20$B!A(B 11:40 | R208 | $BO"B3<0%K<4%(%/%9%H%k!<%@$N(BCFD$B$rMQ$$$?%9%1!<%k%"%C%W2r@O(B
($B%i%$%*%s(B) $B!{(B($B@5(B)$B>.NS(B $BBgM$(B $B!&(B ($B@5(B)$B1JLn(B $BC#@8(B $B!&(B ($B@5(B)$B@>Hx(B $BBs(B $B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$B9b66(B $B9,;J(B $B!&(B ($B%"!<%k%U%m!<(B) ($B@5(B)$BC]ED(B $B9((B | Twin-Screw Extruder CFD Scale-up
| S-39 | 706 |
11:40$B!A(B 12:00 | R209 | $B%,%i%96/2=7O2A(B
($B%]%j%W%i%9%A%C%/%9(B) $B!{(B($B@5(B)$BJ?ED(B $BK.9I(B $B!&(B $B@PED(B $BBg(B $B!&(B $BJ?74(B $B850l(B $B!&(B ($B6eBg(B) ($B@5(B)$BL>2E;3(B $B>MLi(B $B!&(B ($B@5(B)$B3a86(B $BL->0(B | Twin-Screw Extruder Simulation Polymer Compounding
| S-39 | 223 |