$BBh(B 1 $BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B <$B6/2=$5$l$?H?1~!&J,N%%7%9%F%`$NE83+$H(BComputer-Aided Process Engineering$B$N1~MQ(B> | |||||
(9:40$B!A(B10:40) ($B:BD9(B $B>>K\(B $B=(9T(B) | |||||
H103 | $BH?1~%M%C%H%o!<%/$ND69b@:EY46EY7W;;$K$*$1$kDj>o>uBVH?1~J*G;EY$N8zN(E*7hDj(B | Biochemical systems theory complex-step method steady-state sensitivity | S-41 | 157 | |
H104 | DFT$B7W;;$rMQ$$$?:xBNFbJq?(G^$K$*$1$k%Y%s%<%s$N1UAj;@2=3h@-$NM=B,(B | DFT calculation phenol zeolite | S-41 | 567 | |
H105 | Taylor$B12%P%$%*%j%"%/%?!<$rL\;X$7$??tCM%7%_%e%l!<%7%g%s$K$h$kN.F02r@O(B | Taylor vortex flow Turbulence transition Numerical Simulation | S-41 | 205 | |
(10:40$B!A(B11:20) ($B:BD9(B $BC+20(B $B7 | |||||
H106 | $B%P%$%*%W%i%s%H$K$*$1$k1U1UCj=P%W%m%;%90BDj2=5;=Q$N3+H/(B | Liquid-Liquid dispersion Extraction Bioprocess | S-41 | 519 | |
H107 | $B?e@-FsAjN.A`:n$K$*$1$kAX7A@.5sF0M=B,$N$?$a$N%;%0%a%s%H%b%G%k%7%_%e%l!<%7%g%s(B | Simulation Method Flow Monitoring Aqueous Two-Phase Systems | S-41 | 391 | |
(11:20$B!A(B12:00) ($B;J2q(B $BKY9>(B $B9';K(B) | |||||
H108 | [$BE8K>9V1i(B] $BEE6K9=B$@_7W$K$*$1$k(BComputer-Aided Technology | battery porous electrode observation | S-41 | 514 | |
(13:00$B!A(B13:40) ($B;J2q(B $B:y0f(B $B@?(B) | |||||
H113 | [$BE8K>9V1i(B]$BE7A3%,%9$+$i$N?eAG@=B$$N$?$a$N?eAGJ,N%7?%j%U%)!<%^!<(B | hydrogen production membrane reactor hydrogen separation membrane | S-41 | 50 | |
(13:40$B!A(B15:00) ($B:BD9(B $B6bC+(B $B7rEP(B) | |||||
H115 | $B29@tG.$rMxMQ$7$?%P%$%J%j! | combined cycle geothermal energy power generation system | S-41 | 604 | |
H116 | $B>xN1Ec$NCJ8zN($NF0E*JQ2=$K$*$1$k%_%i!<%W%i%s%H%b%G%k$NE,1~J}K!$N8!F$(B | distillation dynamic simulation tray efficiency | S-41 | 561 | |
H117 | $B>xN1J,N%(B-$BH?1~%W%m%;%9%$%s%F%0%l!<%7%g%s$N$?$a$N%J%l%C%8%^%M%8%a%s%H%"%W%m!<%A(B | Process integration Separation reaction Knowledge management | S-41 | 650 | |
H118 | Oscillatory Baffled Membrane Module$B$K$h$kKlJ,N%%W%m%;%9$N6/2=(B | Oscillatory flow Membrane fouling Helical baffle | S-41 | 795 | |
(15:00$B!A(B15:40) ($B;J2q(B $B>>ED(B $B7=8g(B) | |||||
H119 | [$BE8K>9V1i(B] $B%$%*%s1UBN$rMQ$$$??75,%,%95[<}%W%m%;%9@_7W$N$?$a$NJ*@-B,Dj(B | ionic liquid gas adsorption physical properties | S-41 | 113 | |
(15:40$B!A(B17:00) ($B:BD9(B $B2O9g(B $B=( | |||||
H121 | $B%*%$%k%Q!<%`;D^V$N9bB.G.J,2r$K$h$k%P%$%*%$%k@=B$(B:6$B4p$ND>Ns%3%s%G%s%5!<$r;}$DN.F0AXH?1~4o$rMQ$$$F(B | fast pyrolysis oil palm residue fluizided bed | S-41 | 732 | |
H122 | $B%H%j%/%k%Y%C%IH?1~4o$rMQ$$$?&A(B-$B%a%A%k%9%A%l%s?eAG2=$N<~4|JQF0A`:n(B | Periodic operation Trickle bed reactor Mass-transfer | S-41 | 838 | |
H123 | $B%^%$%/%m%j%"%/%?$rMQ$$$?29EYHsDj>oA`:n$N8!F$(B | Microreactor Process Intensification Periodic Operation | S-41 | 307 | |
H124 | $B29EYIT6Q0l>l$K$*$1$k%F%$%i!](B | Taylor-Couette Flow Heat Convection Instability Phenomena | S-41 | 195 | |
$BBh(B 2 $BF|(B | |||||
$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 | |||||
(10:00$B!A(B10:40) ($B:BD9(B $BCfC+(B $B1Q | |||||
H204 | $B?eAG$H;@AG$+$i2a;@2=?eAG$ND>@\9g@.(B | Direct synthesis hydrogen peroxide Catalyst | S-38 | 476 | |
H205 | $BBg5$05%W%i%:%^%j%"%/%?!<$rMQ$$$?%H%k%(%s$N;@2=J,2r(B | Toluene Oxidative decomposition Atmospheric pressure plasma reactor | S-38 | 705 | |
(10:40$B!A(B11:20) ($B:BD9(B $B;38}(B $B=SM:(B) | |||||
H206 | $B%U%m!<%^%$%/%m%j%"%/%?!<$rMQ$$$?@:L)%"%K%*%s=E9g$H$=$N4^%U%CAG%]%j(B $B%^!<9g@.$X$N1~MQ(B | Microreactor Anionic Polymerization | S-38 | 431 | |
H207 | $B82Hy@V30J,8wK!$rMQ$$$?%^%$%/%m?(G^H?1~4o$G$N4D>uC:2=?eAG$NC&?eAGH?1~$NI>2A(B | Infrared Microspectroscopy Microreactor Dehydrogenation | S-38 | 856 | |
(11:20$B!A(B12:00) ($B:BD9(B $B0f>e(B $BJ~Li(B) | |||||
H208 | $B%"%k%^%$%HC4BN$rMQ$$$?%A%e!<%V>u8GDj2=9ZAG%^%$%/%m%j%"%/%?!<$N3+H/(B | microreactor enzyme anodized aluminum | S-38 | 176 | |
H209 | $B%o%$%d!<7?%(%C%A%s%0%"%k%_%K%&%`$rMQ$$$?%^%$%/%m%j%"%/%?!<$N3+H/(B | microreactor methanol steam reforming etced aluminium | S-38 | 178 | |
(13:00$B!A(B13:40) ($B;J2q(B $BKR(B $BBYJe(B) | |||||
H213 | [$BE8K>9V1i(B]API$B@=B$%W%i%s%H$K%^%$%/%m%j%"%/%?!<$rF3F~$9$k0Y$NI,MWMW7o(B | Micro reactor flow reactor manufacturing | S-38 | 453 | |
(13:40$B!A(B14:20) ($B:BD9(B $B5\:j(B $B??:4Li(B) | |||||
H215 | $BIOMOG^:.9g2aDx$N%$%s%I%a%?%7%sB?7A$K5Z$\$91F6A(B | crystal polymorph poor solvent method of operating | S-38 | 751 | |
H216 | $B%^%$%/%mN.BN%G%P%$%9$rMxMQ$7$?>=@OA`:n$K$*$1$k3KH/@8B.EY2r@O(B | Microfluidics Nucleation rate Monodisperse droplets | S-38 | 965 | |
(14:20$B!A(B15:00) ($B:BD9(B $B@nGH(B $BH%(B) | |||||
H217 | $BHy>.1UE)$rMQ$$$?M-5!7k>=$NB?7?@)8f$K$*$1$k2aK0OBEY$N1F6A(B | Polymorphysm Microdroplet Organic crystals | S-38 | 649 | |
H218 | $B%^%$%/%m%A%c%s%M%k$rMQ$$$?EE;R%Z!<%Q! | micro-channel bicolored particle electronic paper | S-38 | 16 | |
(15:00$B!A(B15:40) ($B:BD9(B $B30NX(B $B7r0lO:(B) | |||||
H219 | $BFs=E4I<0J.N.H?1~4o$rMQ$$$?(BBaSO4$B$*$h$S(BFe3O4$B$N9bHfI=LL@Q2=(B | Double-tube type impinging reactor BaSO$4$ Fe$3$O$4$ | S-38 | 204 | |
H220 | $B%^%$%/%m%j%"%/%?!<$rMQ$$$?6bB0%J%NN3;RFbJq%]%j%$%_%IHyN3;R$N:n@=$H$=$N?(G^FC@-(B | metal nanoparticles microreactor polyimide microparticles | S-38 | 546 | |
(15:40$B!A(B16:40) ($B:BD9(B $B@DLZ(B $B@kL@(B) | |||||
H221 | $B5$1U8GH?1~MQ%^%$%/%m%j%"%/%?!<$K$*$1$kN.F0MMAj4Q;!(B | microreactor gas- liquid- solid reaction flow regime observation | S-38 | 229 | |
H222 | $BCf6u>uC:;@%+%k%7%&%`N3;R:n@=$K$*$1$k5$1U@\?(MM<0$N1F6A(B | hollow particle microreactor gas-liquid reaction | S-38 | 960 | |
H223 | Pt$B%J%NN3;R@8@.H?1~$*$h$S?tCMN.BNNO3X7W;;$K$h$k(B2$B1U:.9g>uBVJ,I[I>2A(B | Microreactor Confluence and Bend Mixing | S-38 | 83 | |
$BBh(B 3 $BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B <$B | |||||
(9:00$B!A(B9:40) ($B;J2q(B $BCf;3(B $B9@J?(B) | |||||
H301 | [$BE8K>9V1i(B]$B1U1U%W%m%;%C%7%s%0$X$N%^%$%/%m%j%"%/%?!<$N1~MQ!!(B-$BCj=P$*$h$S2rF}2=(B- | Micro flow chemical prosseing Liquid - luqid exctracion emulsion destroying | S-38 | 452 | |
(9:40$B!A(B10:20) ($B:BD9(B $BEBB<(B $B=$(B) | |||||
H303 | $B%^%$%/%m%G%P%$%9$K$h$kCj=P8zN(8~>e(B | Microreactor Extraction Slug flow | S-38 | 194 | |
H304 | $B2=3XAv@-5!G=$rM-$9$k%"%/%F%#%V%=%U%H%^%?!<$K$h$k4uEZN`6bB0$N<+F0Cj=P(B | Chemotaxis Environmentally-Responsive Function Active Soft Matters | S-38 | 532 | |
(10:20$B!A(B11:00) ($B:BD9(B $B>>2,(B $BN<(B) | |||||
H305 | $BHy>.1UE)$rMQ$$$?%+%j%C%/%9%"%l!<%sM6F3BN$K$h$k6bB0Cj=P%7%9%F%`$N9=C[(B | Microdroplet Solvent extraction Calixarene derivatives | S-38 | 920 | |
H306 | $B%7%/%m%X%-%5%s! | Micro flow chemical prosseing Emulsion destroying Liquid - luqid exctracion | S-38 | 455 | |
(11:00$B!A(B11:40) ($B:BD9(B $BH<(B $B5.I'(B) | |||||
H307 | $B%9%i%0N.$K$h$k%j%A%&%`%$%*%s$N1U1UCj=P!!(B-$BBN@QN.NLHf$N1F6A(B- | Micro channel Slug flow Volumetric mass transfer coefficient | S-38 | 231 | |
H308 | $BHy>.N.O)$G$N1U1UCj=P$K$*$1$kJ* | extraction microchannel mass transfer | S-38 | 600 | |
(11:40$B!A(B12:20) ($B:BD9(B $B@uLn(B $BM32V;R(B) | |||||
H309 | $BAuCV>.7?2=$K8~$1$?5$1U%9%i%0N.$K$h$k%,%95[<}A`:n$N8!F$(B | microreactor slug flow gas absorption | S-38 | 647 | |
H310 | $B05NOB,Dj%G!<%?$rMQ$$$?5$1U%^%$%/%m%j%"%/%?$N%9%i%0D9$5?dDj(B | slug flow microreactor slug length estimation | S-38 | 691 |