$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B |
$BN3;R!&N.BN%W%m%;%9(B |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B2CF#!!Dw?M(B) |
10:00$B!A(B 10:20 | C304 | $B%,%i%9AeMRFb$NN2;@1v@6@!$N?t3X%b%G%k(B ($B00>K;R(B/$B2#9qBg1!(B) $B!{(B($B3X(B)$B?%ED(B $B7r;L(B$B!&(B($B2#9qBg1!(B) ($B@5(B)$B>e%N;3(B $B<~(B | glass tank furnace simulation quality
| S-4 | 9 |
10:20$B!A(B 10:40 | C305 | $B9bG;EY7|By=E9gAe$K$*$1$kMc2sE>?t$N%9%F%C%WA`:n$,%]%j%^!<$NN37BJ,I[$K5Z$\$91F6A(B ($B2#9qBg9)(B) $B!{(B($B3X(B)$B@6?e(B $BJ~H~(B$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 $B<~(B | Suspension polymerization Unsteady mixing operation Particle size distribution
| 2-b | 154 |
10:40$B!A(B 11:00 | C306 | $B<><0G^BN3IYB%_%k$N3F ($B2#9qBg9)(B) $B!{(B($B3X(B)$BLn8}(B $B5AE5(B$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 $B<~(B | Wet grinding Power consumption estimation Grinding rate
| 2-b | 155 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B0f>e!!5AO/(B) |
11:00$B!A(B 11:20 | C307 | $B ($BL>9)Bg(B) $B!{(B($B@5(B)$B2CF#(B $BDw?M(B$B!&(B($B3X(B)$BIpED(B $B9/90(B$B!&(B($B3X(B)$B0/H~(B $BF`J]9a(B$B!&(B($B@5(B)$BB?ED(B $BK-(B$B!&(B($B@5(B)$BD9DE(B $BM:0lO:(B | mixing agitation power number
| 2-b | 4 |
11:20$B!A(B 11:40 | C308 | $BIbM7N3;RYxYBAe$K$*$1$k5$1UJ* ($BElMNBg9)(B) $B!{(B($B3X(B)$BJ!ED(B $BN<(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B | mass transfer aerated stirred tank floating solid particles
| 2-b | 591 |
11:40$B!A(B 12:00 | C309 | $BJ(F-YxYBAe$K$*$1$k29EYJ,I[(B ($BElMNBg9)(B) $B!{(B($B3X(B)$BJ!ED(B $BN<(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B | boiling stirred tank reactor vapour generation
| 2-b | 594 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BBgB?M(B) |
13:00$B!A(B 13:20 | C313 | $B6~6J7?Hy>.%A%c%M%kFb$NN.BN:.9g$K5Z$\$96~6JJ}8~AH9g$;$N1F6A(B ($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B;3El(B $BFF@8(B$B!&(B($B@5(B)$B66K\(B $B=SJe(B$B!&(B($B@5(B)$B0f>e(B $B5AO/(B | Zigzag Channel Microchannel Fluid Mixing
| 2-b | 125 |
13:20$B!A(B 13:40 | C314 | $B;0 ($B:eBg1!4p9)(B) $B!{(B($B@5(B)$B66K\(B $B=SJe(B$B!&(B$B0KF#(B $B42G7(B$B!&(B($B@5(B)$B0f>e(B $B5AO/(B | Fluid Mixing Laminar Flow Isolated Mixing Region (IMR)
| 2-b | 114 |
13:40$B!A(B 14:00 | C315 | $B%j!<%IIU%K!<%G%#%s%0%G%#%9%/$rMQ$$$?Fs<4%9%/%j%e2!=P5!$NMOM;:.N}@-G=(B ($B6eBg9)(B) $B!{(B($B3X(B)$BC]ED(B $B1Q;J(B$B!&(B($B@5(B)$BL>2E;3(B $B>MLi(B$B!&(B($B@5(B)$B3a86(B $BL->0(B$B!&(B($BF|@=9](B) $B=E@P(B $B9b;V(B$B!&(B$BIY;3(B $B=( | Twin-Screw Extruder melt mixing novel kneading element
| 2-b | 98 |
(14:00$B!A(B14:40)$B!!(B($B:BD9(B $B3a86!!L->0(B) |
14:00$B!A(B 14:20 | C316 | $BMc@_CV0LCV$,YxYB$K5Z$\$91F6A(B ($BEl9)Bg9)(B) $B!{(B($B3X(B)$B;3Fb(B $BM:5.(B$B!&(B($BEl9)Bg1!M}9)(B) ($B3X(B)$BJR6M(B $B>-C#(B$B!&(B($B@5(B)$BBg@n86(B $B??0l(B$B!&(B($B@5(B)$B5H@n(B $B;KO:(B$B!&(B($B@5(B)$B>.@n(B $B9@J?(B | mixing power clearance
| 2-b | 449 |
14:20$B!A(B 14:40 | C317 | $B%?!<%S%sMc$rMQ$$$?3IYBAe$N:.9g$K5Z$\$9(Bshear-thinning$B@-$N8z2L(B ($BBgF|K\0u:~(B) $B!{Aj_7(B $B1I$B!&(B($B?@8MBg9)(B) $B:eLn(B $B?-Bg(B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$B:#6p(B $BGn?.(B$B!&(B($B@5(B)$BBgB<(B $BD>?M(B | Shear-thinning fluid Non-Newtonian fluid Mixing time
| 2-b | 408 |
(14:40$B!A(B15:20)$B!!(B($B:BD9(B $BBg@n86!!??0l(B) |
14:40$B!A(B 15:00 | C318 | $B%N%s%(%l%a%s%H%_%-%5!<$N:.9gB%?J$K4X$9$k8!F$(B ($B7D1~5A=NBg(B) $B!{(B($B3X(B)$BQA(B $BA1Z_(B$B!&(B($B3X(B)$BHu8}(B $B>09'(B$B!&(B($B@5(B)$B?"ED(B $BMx5W(B | non-element mixer LIF Mixing enhancement
| 2-b | 181 |
15:00$B!A(B 15:20 | C319 | $B?75,86M}$N:.9g!&J,;6%7%9%F%`(B($B%9%W%l!<%V%l%s%I(B)$B!"%J%NHyN32=A*JL%7%9%F%`$N3567(B ($B%&%$%s%0%?!<%U(B) $B!{(B($B@5(B)$B1)$B!&(B($B:eBg9)(B) $BL1C+(B $B1I0l(B | Nanoparticle generator Spray Blend Mixer Hight-viscosity
| 2-b | 241 |