$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
$B%7%s%]%8%&%`(B $B!c%_%-%7%s%05;=Q$N:GA0@~!d(B |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BNk@n(B $B0l8J(B) |
10:00$B!A(B 10:20 | R104 | $B3IYB1):,$K$h$jM65/$5$l$k@]F0$,AXN.:.9g$K5Z$\$91F6A(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B@nKt(B $BKc5/;R(B $B!&(B ($B@5(B)$B66K\(B $B=SJe(B $B!&(B ($B@5(B)$B0f>e(B $B5AO/(B | Chaos Mixing Streak Lobe Perturbation Effect
| S-39 | 362 |
10:20$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
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B?7Ln(B $B=c0l(B $B!&(B ($B@5(B)$B66K\(B $B=SJe(B $B!&(B ($B@5(B)$B0f>e(B $B5AO/(B | Mixing Streakline Maxblend
| S-39 | 750 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B9b66(B $B9,;J(B) |
11:00$B!A(B 11:20 | R107 | $B9-$$%l%$%N%k%:?tHO0O$rBP>]$H$7$?(BHi-F$B%_%-%5!
($B2#9qBg9)(B) $B!{(B($B3X(B)$B1vC+(B $BD> $B!&(B ($B@5(B)$B;03Q(B $BN4B@(B $B!&(B ($B@5(B)$B?N;V(B $BOBI'(B $B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | eccentric mixing large type impeller mixing energy
| S-39 | 596 |
11:20$B!A(B 11:40 | R108 | $B@55U8r8_2sE>Mc3IYB$K$*$1$kN.BNJQ7AFC@-(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@gED(B $BAa5*(B $B!&(B ($B@5(B)$B8VED(B $B1YG7(B $B!&(B ($B@5(B)$BNkLZ(B $BMN(B | mixing unsteady impeller
| S-39 | 173 |
11:40$B!A(B 12:00 | R109 | $BMpN.0h$K$*$1$kJ?%Q%I%kMcGXLLN.F0@)8fK!$H$=$NFC@-I>2A(B
($BJ!2,Bg9)(B) $B!{(B($B3X(B)$BN6(B $BGnK~(B $B!&(B ($B@5(B)$BNk@n(B $B0l8J(B | Turbulent mixing paddle type impeller power consumption
| S-39 | 393 |
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $B3a86(B $BL->0(B) |
13:00$B!A(B 13:40 | R113 | [$BE8K>9V1i(B] $B:.$<$k2J3X(B
($BL>9)Bg(B) $B!{(B($B@5(B)$B2CF#(B $BDw?M(B | Mixing Agitation Power Consumption
| S-39 | 464 |
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $BBgB<(B $BD>?M(B) |
13:40$B!A(B 14:00 | R115 | $BO"B33IYBAe$rMQ$$$?:.9gA`:n$K$*$1$kG;EY2t%9%1!<%k$N8!F$(B
($B2#9qBg9)(B) $B!{(B($B@5(B)$B?N;V(B $BOBI'(B $B!&(B ($B3X(B)$B0BED(B $B0l51(B $B!&(B ($B@5(B)$B;03Q(B $BN4B@(B $B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | continuous mixing tank reciprocating agitator scale of segregation
| S-39 | 601 |
14:00$B!A(B 14:20 | R116 | $B>e2
($B:4C]2=3X5!3#9)6H(B) $B!{C0@8(B $BFA9T(B $B!&(B $B:4F#(B $B@?(B $B!&(B ($B@5(B)$B:,K\(B $B9M9((B $B!&(B $B6b?9(B $B5W9,(B $B!&(B ($B@5(B)$B2CF#(B $B9%0l(B | Mixing Reciprocal motion CFD
| S-39 | 618 |
14:20$B!A(B 14:40 | R117 | MPS$BK!$rMQ$$$?HsDj>o3IYB$N%7%_%e%l!<%7%g%s(B
($BElKLBgB?858&(B) $B!{(B($B@5(B)$BA>ED(B $BNO1{(B $B!&(B ($B@5(B)$B2CG<(B $B=cLi(B $B!&(B ($B@5(B)$Bc7F#(B $BJ8NI(B | MPS simulation mixing
| S-39 | 456 |
(14:40$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 | $B79
($B;37ABg1!M}9)(B) $B!{(B($B@5(B)$BLg3p(B $B=( $B!&(B ($B@5(B)$B86ED(B $B1QFs(B $B!&(B ($B@5(B)$B7*;3(B $B2mJ8(B | Agitated vessel mass transfer Mixing
| S-39 | 390 |
16:20$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 |