| $B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B |
|---|---|---|---|---|---|
| $B%7%s%]%8%&%`(B $B!c2=3X%W%m%;%9$N6/2=$rL\;X$7$?%@%$%J%_%C%/$JH?1~$H0\F08=>]$N1~MQ!d(B | |||||
| (9:00$B!A(B10:00)$B!!(B($B:BD9(B $B5H@n;KO:(B) | |||||
| S101 | $B%^%$%/%m%A%c%s%M%kFb$NN3;R4V$*$h$SN3;RJILL4V>WFM8=>]$N5<;wE*(BDNS$B2r@O(B | microchannel particle collision | S-5 | 474 | |
| S102 | $B?tCM%7%_%e%l!<%7%g%s$K$h$kB?AX%U%#%k%`MOM;2!=P%W%m%;%9$NG4CF@-2r@O(B | multi-layer film coextrusion polymer melt flow | S-5 | 767 | |
| S103 | CO2$B2=3X5[<}%W%m%;%9$K$*$1$k1UB&J* | chemical absorption carbon dioxide mass transfer coefficient | S-5 | 833 | |
| (10:00$B!A(B11:00)$B!!(B($B:BD9(B $B2O9g=( | |||||
| S104 | $B%^%$%/%m%A%c%M%k$rM-$9$k%/%m%9%U%m(B-$B8B30_I2aAuCVFb$N0\F08=>](B | Microchannel Ultrafiltration Cross Flow | S-5 | 628 | |
| S105 | $B3J;R%\%k%D%^%sK!$K$h$k(BCarreau$B%b%G%kN.BNN.$l$N?tCM2r@O(B | Lattice Boltzmann method Shear-thinning fluid Carreau model | S-5 | 705 | |
| S106 | $B1UE)$N>WFM$rH<$&5$1U3&LL$rDL$7$F$NJ* | mass transfer air-water interface droplet | S-5 | 39 | |
| (11:00$B!A(B12:00)$B!!(B($B:BD9(B $B>>7(MN2p(B) | |||||
| S107 | $B9bG4@-N.BNCf$NHyN3;RJ,;65sF0$K4X$9$k%b%G%k2r@O(B | dispersion characteristics of fine particles model analysis | S-5 | 435 | |
| S108 | $B@P3%F}@=B$%W%m%;%9$K$*$1$k%9%i%j!<$NG4EY0[>o$K4X$9$k8&5f(B | Lime milk Slurry Rheology | S-5 | 831 | |
| S109 | $B3&LL3h@-:^$K$h$k93NO8:>/N.$l$NEAG.FC@-(B | Drag reduction Heat transfer Surfactant | S-5 | 850 | |
| (13:00$B!A(B14:00)$B!!(B($B:BD9(B $BBg?9N4IW(B) | |||||
| S113 | $B%W%m%;%9;~7ONs2hA|$N%/%i%9%?%j%s%0$K$*$1$k%G!<%?JQ49 | clustering process monitorng pattern processing | S-5 | 58 | |
| S114 | $BN.2CG]M\%7%9%F%`$NF0E*46EY2r@O(B | dynamic sensitivity fed-batch culture Penicillin | S-5 | 250 | |
| S115 | $B%^%$%/%mN.O)$K$*$1$k1U1U%9%i%0N.$rMQ$$$?:.9g!&Cj=P$N?WB.2=(B | Liquid-liquid slug flow Internal circulation flow Microchannel | S-5 | 22 | |
| (14:00$B!A(B14:40)$B!!(B($B;J2q(B $B9uED@i=)(B) | |||||
| S116 | [$BE8K>9V1i(B]$B>J%(%M%k%.!<$r%?!<%2%C%H$H$7$?%W%m%;%96/2=$NE83+(B | energy savings process intensification heat-integrated distillation | S-5 | 641 | |
| (14:40$B!A(B16:00)$B!!(B($B:BD9(B $B@DLZ@kL@(B) | |||||
| S118 | $B8GBN9bJ,;R7?G3NAEECS$NF0FC@-$*$h$S@)8f$N8!F$(B | PEFC Dynamics Control | S-5 | 315 | |
| S119 | $B%^%$%/%mN.O)Fb1U1UFsAjN.$l$K$*$1$k05NOJQF07WB,$H3&LL$N0BDj@-2r@O(B | micro channel two-phase flow pressure | S-5 | 13 | |
| S120 | Y$B;z7?%^%$%/%mN.O)Fb$K$*$1$k1U!9FsAj%9%i%0N.$KM?$($kN.B.$N1F6A(B | microchannel slug flow two-phase flow | S-5 | 523 | |
| S121 | $B?eMO1U$K$*$1$kEE5$N.BNNO3X$r1~MQ$7$?%b!<%?$N3+H/(B | electrohydrodynaamics motor water | S-5 | 336 | |
| (16:00$B!A(B17:00)$B!!(B($B:BD9(B $BNkLZ(B $BMN(B) | |||||
| S122 | $B?tCM2r@O$rMQ$$$?(BTaylor$B12$NN.BN2r@O(B | Taylor Vortex Flow Analysis | S-5 | 866 | |
| S123 | $B%"%9%Z%/%HHf$N>.$5$$(BTaylor$B12$K$h$k8G1U:.9gAj$N_I2a | Taylor vortex flow Reynolds number Cake layer | S-5 | 229 | |
| S124 | Taylor-couette$B12N.$l$K$*$1$kA}?#FC@-(B | Taylor-couette vortex flow spirulina chlorophyll | S-5 | 910 | |
| (17:00$B!A(B18:00)$B!!(B($B:BD9(B $BCf4d(B $B>!(B) | |||||
| S125 | PEG$BB8:_2<$K$*$1$kEE3&A`:n$K$h$kAj7A@.$NB%?J(B | Alternate current Polyethylene glycol Phase | S-5 | 65 | |
| S126 | $B%l!<%682Hy6@$rMQ$$$?@\?(>uBV2<$NN3;RI=LL$ND>@\4Q;!(B | heat transfer surface roughness thermal resistance | S-5 | 1001 | |
| S127 | $B1U(B-$B1UCj=P7O$K$*$1$k(BMarangoni$B8z2L$K$h$k3&LL3IMp$N7ABV(B | liquid-liquid extraction Marangoni effect mass transfer | S-5 | 681 | |
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