$B:G=*99?7F|;~!'(B2020-09-26 15:59:01
Data-utilization (2$B7o(B) | ||||
---|---|---|---|---|
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
199 | [$B>7BT9V1i(B] $B=;M'2=3X$K$*$1$k%G!<%?2r@O5;=Q$N3hMQ(B | SS-7 | Data-utilization analysis Cultivate | 12/18 15:41:17 |
209 | [$B>7BT9V1i(B] $B=;M'2=3X$K$*$1$k%G!<%?2r@O5;=Q$N3hMQ(B | SP-9 | Data-utilization analysis Cultivate | 12/18 16:26:16 |
Database (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
581 | $B%$%*%s1UBN$NEE;R>uBV%G!<%?%Y!<%99=C[$H%,%95[<}G=I>2A$X$N1~MQ(B | 1-a | Ionic liquid Database Machine learning | 12/21 13:18:36 |
DBD (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
382 | P/L$BH?1~$K$*$1$k(BNH3$B@8@.A*Br@-$r8~>e$9$kM6EEBN2~JQ%P%j%"J|EE(B | 5-c | ammonia DBD | 12/20 11:04:49 |
DDS (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
543 | $B?75,$J(BDDS$B%-%c%j%"$r;X8~$7$?(BCubosome$B=89gBN$ND4@=$HI>2A(B | 12-c | Cubosome DDS Membrane Characterization | 12/20 21:29:06 |
Dealcoholization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-10 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
257 | [$B>7BT9V1i(B] $B%S!<%kMQ(B $BC&%"%k%3!<%k%7%9%F%`(B($BKlJ,N%5;=Q(B) | SP-10 | Dealcoholization Minimum Aroma loss No heating | 12/19 10:40:13 |
Decarbonization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
176 | [$B>7BT9V1i(B] $B>-Mh$N%(%M%k%.!<%7%9%F%`$K$*$1$k?eAG%(%M%k%.!<$X$N4|BT(B | SS-1 | Hydrogen Energy System Decarbonization | 12/18 12:56:39 |
Decision making (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
461 | $BO"B3!&%P%C%AJ}<0$r9MN8$7$?Cm | 6-b | Pharmaceutical manufacturing Decision making Process modeling | 12/20 16:56:30 |
Decision support method (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
532 | $B86Lt@=B$$K$*$1$k%P%C%A!&%U%m!<9g@.$NA*Br;Y1g | 6-b | Pharmaceutical manufacturing Decision support method Batch and flow syntheses | 12/20 20:25:00 |
Decomposition (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-i (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
653 | $BD62;GH$rMQ$$$?%H%j%/%m%m%(%A%l%s(B(TCE)$B$NJ,2r%a%+%K%:%`$N2rL@(B | 13-i | TCE Ultrasound Decomposition | 12/22 01:20:18 |
decontamination soil (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-i (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
564 | $B=|@wEZ>m$NJ| | 13-i | decontamination soil Cs removal FSI salt | 12/21 01:20:53 |
Deep eutectic solvents (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
165 | $B6(F1Cj=P8z2L$K4p$E$/?<6&>=MOG^$NAO@=$H%j%A%&%`Cj=P$X$N1~MQ(B | 4-f | Deep eutectic solvents Lithium | 12/18 10:47:28 |
Defluidization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
324 | $B%,%9$N5[Ce$K$h$C$F0z$-5/$3$5$l$k0l;~E*$JHsN.F02=8=>]$N2r@O(B | 2-c | Fluidized bed Defluidization Adsorption | 12/19 17:08:18 |
defluorination (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
493 | $B1v4p@-G.?e$rMQ$$$?(BFluorobenzene$B$NC&%U%CAG2=$NH?1~5!9=(B | 8-d | hydrothermal defluorination fluorobenzene | 12/20 18:31:10 |
Degassing (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
164 | $B?e$ND62;GHC&5$$X$N<~GH?t$N1F6A(B | 5-b | Ultrasonic Degassing Cavitation | 12/18 10:46:10 |
dehydrated Portland cement (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
765 | $BC&?e%;%a%s%H$N:F?eOB2aDx$G$N3&LL7kCe@-$NIT2sI|MW0x$K$D$$$F(B | 12-a | dehydrated Portland cement rehydration interfacial breakoff | 12/22 21:09:17 |
Dehydration (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
433 | $BCf6u;eC:AGKl$N3F | 4-a | carbon membrane dehydration organic solvent | 12/20 15:25:23 |
504 | $B%P%$%*%V%?%N!<%kH/9Z$X$NL55!B?9& | 4-a | Membrane separation Butanol Dehydration | 12/20 18:51:38 |
Dehydrogenation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
723 | Fe$B7O?(G^$N3J;RN22+$r3hMQ$7$?Dc5i%"%k%+%s(B(C2-C4)$B$NC&?eAG(B:$B5$Aj(BH2S$B$NB%?J8z2L(B | 5-a | Hydrogen sulfide Dehydrogenation Fe | 12/22 16:36:04 |
Delay risk analysis (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
234 | $B%W%m%8%'%/%H!&%9%1%8%e!<%k$NCY1d%j%9%/$NDjNLJ,@O | 6-f | Schedule network Delay risk analysis Rescheduling | 12/18 18:48:15 |
Density (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
225 | $BFs;@2=C:AG(B/$B%a%?%N!<%kFs@.J,7O:.9gN.BNL)EY$NB,Dj$HAj4X(B | 1-a | Methanol Carbon dioxide Density | 12/18 17:29:17 |
Density Functional Theory (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
336 | DFT$B7W;;$r%Y!<%9$H$7$?%O%i%$%I%Z%m%V%9%+%$%HNL;R%I%C%HH/8wGHD9$NM=B,(B | 12-d | Perovskite Density Functional Theory | 12/19 18:56:59 |
444 | $B%j%A%&%`6u5$EECS%+%=!<%I6K$KMxMQ$9$kFs857O;@2=J*?(G^$NM}O@C5:w(B | 5-a | binary oxide catalysts lithium-air battery density functional theory | 12/20 16:18:50 |
617 | $B8GBNI=LL4V$NAB1U@-0zNO$H1U2M660zNO$N(BDFT$B7W;;(B | 12-a | Surface forces Capillary-induced phase transition Density functional theory | 12/21 17:37:15 |
density gradient (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
521 | $BF}@.J,$r4^$`0{NA$+$i$NHy@8J*8!=P$K8~$1$?A0=hM}J}K!$N8!F$(B | 7-c | bacteria separation milk density gradient | 12/20 19:35:47 |
dental materials (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
442 | $B0[7AL55!HyN3;R$ND4@=$H;u2J:`NA$X$N1~MQ(B | 12-c | microsphere dental materials filler | 12/20 16:01:34 |
dephosphorization slag (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
13 | $B3F;@MOG^$K$h$kC&%j%s%9%i%0$+$i$N%j%s$NG;=L(B | 13-e | dephosphorization slag phosphorus recovery acid treatment | 11/25 10:30:10 |
Depletion force (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
760 | $B8O3i0zNO$,M65/$9$k%3%m%$%I<+8J=8@Q5!9=$N2rL@(B | 12-a | Self-assembly Colloid Depletion force | 12/22 20:58:45 |
depolymerization (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
332 | $BG.?e>r7o2<$K$*$1$k(Bpoly(butylene terephthalate)$B$N2r=E9g$K$*$h$\$9E:2C%"%_%s | 8-d | poly(butylene terephthalate) depolymerization hydrothermal | 12/19 17:34:54 |
677 | poly(L-lactic acid)$B$N2r=E9g$K$*$1$k(Blactic acid$B<}N($K5Z$\$9H?1~29EY!"(BpH$B$N1F6A(B | 13-e | poly(L-lactic acid) depolymerization basic aqueous solution | 12/22 11:03:04 |
deposition (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-m (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
704 | $B%7%j%+HyN3;R$N1UAjCf$G$NBO@Q8=>]$N4pACE*8!F$(B | 12-m | silica fine particles deposition liquid phase | 12/22 14:55:00 |
705 | $B5$1U3&LL$K$*$1$k%(%"%m%>%k$ND@Ce$H$=$N:YK&1~Ez(B | 2-f | Aerosol Deposition | 12/22 14:56:53 |
Depressurization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B K-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
384 | [$B>7BT9V1i(B] Natural gas hydrates as an energy resource -Development of gas production methods based on its reservoir properties | K-1 | Methane hydrate Depressurization Permeability | 12/20 11:14:29 |
Design (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
649 | $BB?4I<0G.8r497?%^%$%/%m%j%"%/%?%b%8%e!<%k@_7WK!(B | 5-f | Microreactor Design CFD | 12/21 23:47:11 |
Design and optimization (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B K-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
85 | Integrating Life Cycle Assessment for Design and Optimization of CO2 Utilization Process | IS-1 | Life Cycle Assessment Design and Optimization CO2 Utilization Process | 12/12 16:39:15 |
800 | [$B>7BT9V1i(B] Redox Flow Batteries for Large-scale Electrical Energy Storage: The Third Generation | K-3 | Redox flow battery Porous electrode Design and optimization | 12/22 23:48:28 |
Deterioration (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
628 | $B1x@wEZ>mEy$ND94|2>CV$KH<$&J]4IMF4o$NNt2=$K4X$9$kD4::(B | 13-c | Flexible container Deterioration Long-term storage | 12/21 19:07:47 |
dewetting (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-h (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
452 | [$BM%=(O@J8>^(B] $B%3%s%]%8%C%HGvKl$N(Bdewetting$B5sF0$K5Z$\$9%J%NN3;R$NI=LL=$>~:?$N1F6A(B | 12-h | nanocomposite thin film dewetting surface modifier | 12/20 16:38:31 |
Diagnostics (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
212 | [$B>7BT9V1i(B] $BG.G^%\%$%i! | SP-9 | Hot oil heater Heat transfer oil Diagnostics | 12/18 16:32:10 |
Diamond-like carbon (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-m (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
512 | $BDcK`;$(BDLC$BKl>e$X$N%]%j%^! | 12-m | Diamond-like carbon Molecular Dynamics Polymethacrylate(PMA) | 12/20 19:02:15 |
Die filling (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
697 | $B?tCM%7%_%e%l!<%7%g%s$K$h$k%^%k%A%-%c%S%F%#6b7?$X$NJ4Kv= | 6-e | Discrete Element Method Computational Fluid Dynamics Die filling | 12/22 14:28:46 |
dielectric constant (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
356 | $BM6EEN($H0BDj@-$r9MN8$7$?9bJ,;R:`NA$N%b%N%^!<9=B$$N@_7W(B | 6-e | polymer dielectric constant glass transition temperature | 12/19 23:54:07 |
Dielectric particle layer (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
448 | $BN3;R$N;g30@~>H | 2-f | Photoelectric charging Dielectric particle layer Particle motion analysis | 12/20 16:32:49 |
different frameworks (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
240 | 3$B | 4-f | New extraction reagent different frameworks metal extraction | 12/18 20:36:47 |
differentiation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
699 | $BCf6u;eFb;0u8z2L(B | 7-e | iPS cells differentiation three-dimensional culture | 12/22 14:30:33 |
Diffusion coefficient (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (2$B7o(B), 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
412 | $B%I%i%C%0%G%j%P%j!<%7%9%F%`MQ%]%jF};@(B-$B%]%j%S%K%k%T%m%j%I%sJ?Kl$N3H;6F)2a@-$NI>2A(B | 7-e | Drug delivery system Controlled release Diffusion coefficient | 12/20 14:06:09 |
559 | $B%]%j%V%A%k%a%?%/%j%l!<%H(B+$B%"%k%3!<%kN`$N3H;678?t$NB,Dj$HAj4X(B | 1-a | measurement correlation diffusion coefficient | 12/20 23:49:23 |
784 | Taylor$BK!$K$h$k9b05Fs;@2=C:AG(B+hexane$B:.9gN.BNCf$N(Bbenzene$B$N3H;678?t$NB,Dj$H?d;;(B | 1-a | mixture of CO2 and hexane diffusion coefficient benzene | 12/22 22:37:29 |
diffusion coefficients (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B HQ-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
686 | [$B0MMj9V1i(B] $BNL;R2=3X7W;;$+$iF@$i$l$kJ,;RBN@Q$rMQ$$$?Aj8_3H;678?t$N?d;;K!(B | HQ-21 | molecular volume diffusion coefficients quantum chemical calculation | 12/22 12:39:48 |
diffusion/reaction kinetics (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
230 | $B%"%s%b%K%";@2=:Y6]8GDj2=%2%kN3;RCf$N;@AG$N3H;6$HH?1~$NB.EYO@(B | 12-e | ammonia-oxidizing bacteria calcium alginate gel diffusion/reaction kinetics | 12/18 17:42:09 |
diffusivity (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B K-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
734 | Cu(tmhd)2$B$N9b29D6NW3&(BH2/CO2$B:.9gN.BNCf$K$*$1$k3H;678?t$NI>2A(B | 8-d | Diffusivity Metal Organics Supercritical H2/CO2 Mixture | 12/22 18:11:34 |
769 | [$B>7BT9V1i(B] PEMFC modeling based on characterization of effective diffusivity in cathode catalyst layer | K-3 | PEMFC catalyst layer diffusivity | 12/22 21:28:04 |
Digital (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
194 | [$B>7BT9V1i(B] $B;0I)%1%_%+%k$K$*$1$k(BDX$B5;=Q$N8!F$5Z$S?M:`0i@.$X$N | SS-7 | Digital Transformation Training | 12/18 15:18:04 |
207 | [$B>7BT9V1i(B] $B;0I)%1%_%+%k$K$*$1$k%G%8%?%k%H%i%s%9%U%)!<%a!<%7%g%s$N | SP-9 | Digital Transformation AI | 12/18 16:16:57 |
Dimensional analysis (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
173 | [$B>7BT9V1i(B] $B:F@82DG=%(%M%k%.! | SS-1 | Dimensional analysis 2D manufacturing SDGs | 12/18 12:50:21 |
dimensionless moduli (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
638 | $B8GBN9bJ,;RG3NAEECS$NJ,6K6J@~$N;@AGJ,050MB8@-$+$i$NL5 | 9-e | polymer electrolyte fuel cell analysis method dimensionless moduli | 12/21 20:05:08 |
Dimethyl ether (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
516 | $B;n:n%W%i%s%H$rMQ$$$?<>=aHy:YAtN`$+$i$NL};i$N1U2=%8%a%A%k%(!<%F%kCj=P(B | 8-f | Dimethyl ether Biofuel Microalgae | 12/20 19:22:39 |
dimethyl sulfoxide (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-i (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
10 | $BM-5!2&?e$rMQ$$$?2+F<9[(B (CuFeS2) $B?;=P%W%m%;%9$N3+H/(B | 13-i | hydrometallurgy chalcopyrite dimethyl sulfoxide | 11/21 17:19:20 |
83 | $B%8%a%A%k%9%k%[%-%7%I(B(DMSO)$B$NG.J,2rCf4V@8@.J*$NJ,@O(B | 10-h | Dimethyl Sulfoxide Intermediate Product Thermal Decomposition | 12/12 15:08:22 |
diphosphonic acid (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
244 | $B?75,%8%[%9%[%s;@7OCj=P;nLt$N3+H/$H4uEZN`6bB0%$%*%s$NCj=P(B | 4-f | diphosphonic acid solvent extraction rare earth | 12/19 08:14:59 |
dipole moment (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
125 | $BJ,;RF0NO3X%7%_%e%l!<%7%g%s$K$h$k%Q%i%U%#%s(B+$B%"%k%3!<%k7O$N5$1UJ?9U(B | 1-a | radial distribution function dipole moment intermolecular potential | 12/17 11:00:04 |
Direct formate fuel cell (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
611 | $BG3NA3H;6$r9MN8$7$?D>@\%.;@1vMO1U7?8GBN%"%k%+%jG3NAEECS%b%G%k$N9=C[(B | 9-e | Direct formate fuel cell Mathematical model Fuel transport | 12/21 16:38:34 |
Direct formate solid alkaline fuel cell (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
717 | $B9bBQ5W%(!<%F%k%U%j! | 9-e | Direct formate solid alkaline fuel cell Anion conducting membrane Ether-free aromatic polymer | 12/22 16:14:17 |
direct observation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
495 | $BL}Cf?eE)$K$h$C$FIuF~$5$l$?%R%I%m%-%7%W%m%T%k%;%k%m!<%9$NF0E*5sF0(B | 12-b | thermo-induced dynamics direct observation | 12/20 18:35:17 |
Direct partial oxidation of methane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
88 | $B%<%*%i%$%HC4;}5.6bB0?(G^>e$G$N%a%?%sD>@\ItJ,;@2=H?1~$K$h$k(BC1$B4^;@AG2=9gJ*9g@.(B | 5-a | Direct partial oxidation of methane zeolite precious metal | 12/13 14:56:28 |
Dirt process (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-10 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
258 | [$B>7BT9V1i(B] $B1x$l(B($BJD:I(B)$B7O%W%m%;%9$X$ND)@o(B!$BO"B31?E>$r2DG=$K$9$k9b@-G=%G%#%9%H%j%S%e!<%?!<$NFCD'$K$D$$$F(B | SP-10 | Packed Column Dirt process High-performance distributors | 12/19 10:46:18 |
discharge flow rate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
678 | 2$BCJ%G%#%9%/%?!<%S%sMc$*$h$S%Q%I%kMc$NEG=PN.NL(B | 2-b | discharge flow rate disk turbine impeller paddle impeller | 12/22 11:08:56 |
Discrete Element Method (4$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-f (2$B7o(B), 6-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
60 | $BA48GBNEECS$N | 2-f | Discrete Element Method Packing structure Powder compression | 12/5 17:20:46 |
122 | DEM$B%7%_%e%l!<%7%g%s$K$h$k%j%\%s%_%-%5!<$NJ4BN:.9g:GE,2=%Q%i%a!<%?$NCj=P(B | 2-d | Discrete Element Method Ribbon mixer Mixing mechanism | 12/16 20:35:32 |
154 | $B0l<405=L;n83$K$*$1$kC10l@.J,$H(B2$B@.J,$NJ4:UFC@-$NHf3S8!F$(B | 2-f | Binary system grinding Uniaxial compression Discrete Element Method | 12/17 18:16:29 |
697 | $B?tCM%7%_%e%l!<%7%g%s$K$h$k%^%k%A%-%c%S%F%#6b7?$X$NJ4Kv= | 6-e | Discrete Element Method Computational Fluid Dynamics Die filling | 12/22 14:28:46 |
disk turbine impeller (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
678 | 2$BCJ%G%#%9%/%?!<%S%sMc$*$h$S%Q%I%kMc$NEG=PN.NL(B | 2-b | discharge flow rate disk turbine impeller paddle impeller | 12/22 11:08:56 |
Dispersibility (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
79 | $B%(%A%l%s%0%j%3!<%k$r | 9-b | Nanofluid Heat transfer coefficient Dispersibility | 12/12 08:35:27 |
298 | $B:YK&Fb4Q;!$X8~$1$?7V8w<'@-J#9gN3;R$NJ,;6!&6E=8@)8f(B | 12-c | magnetic nanoparticles fluorescence dispersibility | 12/19 14:11:28 |
dispersion (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 3-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
105 | $B?e7O%+!<%\%s%9%i%j!<$K$*$1$k9bJ,;RE:2C:^$N5[Ce5sF0$,EE6KFC@-$K$*$h$\$91F6A(B | 12-k | Adsorption Dispersion Carbon | 12/16 10:59:31 |
424 | $BBg5$05%W%i%:%^=hM}(BPTFE$BJ4Kv$rMQ$$$?(BFC$B%,%93H;6AX$N:n@.(B | 3-b | Plasma PTFE dispersion | 12/20 14:53:27 |
471 | $BAjJ,N%7?(BCO2$B5[<}:^$N5[<}FC@-$K5Z$\$9E:2C:^$N1F6A(B | 4-d | phase separation CO2 absorption dispersion | 12/20 17:18:48 |
Dispersion Stability (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
6 | $B9bJ,;R$r9=@.$9$k41G=4p$,HyN3;RJ,;60BDj@-!$Hy@8J*FG@-$KM?$($k1F6A(B | 12-a | Polymer Particle Dispersion Stability Antimicrobial Activity | 11/14 08:50:28 |
disrupted sludge (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
361 | [$BM%=(O@J8>^(B] $BL55!1v$NCJ3,E*E:2C$K$h$kGK:U1xE%$ND@9_@-G=$N8~>e(B | 4-b | settling flocculation disrupted sludge | 12/20 09:40:37 |
Dissociation temperature (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
714 | CH4/N2$B:.9g%,%9%O%$%I%l!<%H$N(BTetrahydrofuran$BE:2C$K$h$k2rN%29EY$X$N1F6A(B | 1-a | Hydrate Separation Dissociation temperature | 12/22 15:49:57 |
Dissolution (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
544 | $BD@EBK!$K$h$k;@2=0!1tJ4Kv$N9g@.$H$=$NMO2r5sF0(B | 12-g | Powder Synthesis Dissolution | 12/20 21:31:23 |
Dissolution rate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
626 | $B6&>=7O$rMxMQ$7$?MO2rB.EY2~A1$N$?$a$N8GAjJ,;6M;1U>=@OK!(B | 12-g | Melt crystallization Eutectic Dissolution rate | 12/21 18:59:38 |
Distillation (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-8 (2$B7o(B), HC-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
39 | [$B>7BT9V1i(B] $B%7%j%+7OJ,N%Kl$N(BMolecular-Net-Sieving$B@)8f$H1UAj$*$h$S5$Aj7OJ,N%$N9bEY2=(B | SS-8 | distillation packed column energy saving | 12/2 16:18:56 |
40 | [$B>7BT9V1i(B] $B5,B'= | SS-8 | distillation packed column energy saving | 12/2 16:24:42 |
99 | [$B0MMj9V1i(B] $B%H%j%A%&%`?e$NE,@Z$J=hM}$K$D$$$F(B | HC-14 | Tritium Fukushima Distillation | 12/15 14:33:14 |
distributed generation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
541 | $B7OE}6(D4!?J,;67?%(%M%k%.!<%7%9%F%`3+H/$K8~$1$?5!3#3X=,$K$h$kEENO<{MW$N=E2s5"J,@O(B | 9-e | distributed generation renewable energy machine learning | 12/20 21:03:55 |
distribution coefficient (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-h (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
93 | $B%b%G%k?)IJ$KBP$9$k%0%k%3!<%9$*$h$S1v2=%J%H%j%&%`$NJ,G[78?t$KM?$($k29EY$N1F6A(B | 7-h | distribution coefficient food seasoning | 12/13 19:03:35 |
Dividing wall distillation column (DWDC) (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
208 | Controllability comparison of the four-product Petlyuk dividing wall distillation column using temperature control schemes | 4-c | Dividing wall distillation column (DWDC) Simplified temperature difference control (STDC) Simplified double temperature difference control (SDTDC) | 12/18 16:25:55 |
dividing-wall distillation column (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
148 | A kind of topological structures of vapor recompressed dividing-wall distillation columns | 4-c | dividing-wall distillation column vapor recompressed heat pump process design | 12/17 17:08:53 |
DO-stat (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
503 | Factors affecting anti-CRP scFv production using E. coli by DO-stat fed-batch culture | 7-a | DO-stat Fed-batch culture scFv | 12/20 18:49:29 |
doping (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
239 | $B6bB0%I!<%W(BTiO2$B5e>uB?9&BN$N9g@.$H?(G^E*(BCO2$B%a%?%s2=H?1~(B | 12-d | TiO2 doping catalyst | 12/18 19:59:04 |
Double emulsion (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
391 | $B%@%V%k%(%^%k%7%g%s@8@.$K%^%$%/%mN.O)$NN.O)7A>u$HMO1UJ*@-$,M?$($k1F6A(B | 12-b | Double emulsion Flow focusing | 12/20 12:05:56 |
Drag coefficients (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
434 | Front-Tracking$BK!$K$h$kC10l1UE)$N?tCM2r@O(B | 2-a | Front-Tracking Drag coefficients droplets | 12/20 15:26:12 |
Drag reduction (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
561 | $B3&LL3h@-:^$K$h$kDq93Dc8:8z2L$NCOCfG.MxMQ%7%9%F%`$X$NE,MQ(B | 2-a | Geothermal utilization Drag reduction Surfactant | 12/21 00:17:40 |
793 | [$B0MMj9V1i(B] $B%l!<%6!<%I%C%W%i!<$;$sCG1~NO7WB,K!$N3+H/$K$h$k5$K"N.$K$*$1$kK`;$Dq93$NI>2A(B | HQ-21 | Shear stress Turbulent flow Drag reduction | 12/22 23:25:43 |
draw solute (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
379 | $B29EY1~Ez@-%]%j%"%k%-%l%s%0%j%3!<%k$N(BFO$B6nF0MO1U$H$7$F$NFC@-I>2A$HJ,;RNL$N1F6A(B | 4-a | thermoresponsive forward osmosis draw solute | 12/20 10:37:08 |
DRM (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
73 | Nickel-based Hybrid Nanostructure as High-Performance Catalysts for Dry Reforming of Methane | 12-c | Aerosol nanostructure DRM | 12/10 11:32:06 |
drop tube furnace (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
61 | $B%j%"%/%?%M%C%H%o!<%/2r@O$K$h$kHyJ4C:G3>F$NH?1~FC@-I>2A(B | 9-c | chemical kinetics NOx drop tube furnace | 12/5 17:35:58 |
Droplet formation (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
91 | $B%$%s%/%8%'%C%H%N%:%k$+$i$N1UE)EG=P%7%_%e%l!<%7%g%s(B | 2-a | inkjet nozzle droplet formation VOF | 12/13 17:22:22 |
525 | $BB?9&@-4p:`$rE}9g$7$?%^%$%/%mN.BN%G%P%$%9$rMQ$$$k1UE)7A@.$N@)8f(B | 2-e | Droplet formation Microfluidic device Emulsification | 12/20 19:51:55 |
Droplet impact (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
81 | $B@\?(3Q$N%b%G%k$r9MN8$7$?1UE)$NJILL$X$N>WFM$K4X$9$k?tCM2r@OE*8!F$(B | 2-e | Volume of fluid Droplet impact Contact angle | 12/12 11:30:29 |
droplets (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
434 | Front-Tracking$BK!$K$h$kC10l1UE)$N?tCM2r@O(B | 2-a | Front-Tracking Drag coefficients droplets | 12/20 15:26:12 |
Drug carrier (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B HQ-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
259 | [$B0MMj9V1i(B] $BB?9&@-G[0L:xBNN3;R$N0eLtJ,Ln$X$N1~MQ2DG=@-(B | HQ-21 | Metal-organic framework Porous coordination polymer Drug carrier | 12/19 10:50:50 |
Drug Delivery (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
429 | $B%"%k%D%O%$%^! | 7-e | Drug Delivery Nanoparticles Amyloid | 12/20 15:08:33 |
Drug delivery system (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
142 | $B8w;@H/@8:^$rFbJq$7$?(BpH$B1~Ez@-%O%$%I%m%2%k$+$i$NLtJ*$N@)8fJ|=P(B | 12-e | pH-responsive hydrogel drug delivery system photo acid generator | 12/17 16:23:32 |
412 | $B%I%i%C%0%G%j%P%j!<%7%9%F%`MQ%]%jF};@(B-$B%]%j%S%K%k%T%m%j%I%sJ?Kl$N3H;6F)2a@-$NI>2A(B | 7-e | Drug delivery system Controlled release Diffusion coefficient | 12/20 14:06:09 |
drug screening (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
89 | $B:YK&2hA|2r@O5;=Q$rMQ$$$??@7PJ]8n2=9gJ*$N%W%m%U%!%$%j%s%0(B | 7-a | drug screening cell image analysis | 12/13 15:26:59 |
Dry Powder Inhalation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
761 | $BJ4Kv5[F~@=:^$NGYE~C#5sF0$K$*$1$kN3;RIUCe8=>]$N2r@O(B | 2-f | Dry Powder Inhalation Numerical simulation particle behavior | 12/22 20:58:59 |
Dry reforming of methane with CO2 (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B HQ-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
662 | [$B0MMj9V1i(B] $BG.!&J* | HQ-21 | Catalytic wall plate reactor Assembly-type microreactor Dry reforming of methane with CO2 | 12/22 07:54:42 |
drying (5$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-h (5$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
107 | $BN.F0AXFb$KA^F~$7$?<>$j:`NA$N4%AgFC@-$K5Z$\$98:0505NO<~4|JQF0$N1F6A(B | 4-h | drying pressure change fluidized bed | 12/16 12:17:21 |
108 | $B8:052aG.?e>x5$N.F0AXFb$KA^F~$7$??)IJ86NA$N4%Ag(B | 4-h | drying superheated steam fluidized bed | 12/16 12:23:07 |
109 | $BDc29EYN.F0AX$KA^F~$7$?E`7k:`NA$N4%Ag(B | 4-h | drying frozen material fluidized bed | 12/16 12:30:02 |
127 | $B8:05Dc29EY6u5$=[4D$K$h$kE`7k?)IJ86NA$N4%AgFC@-(B | 4-h | drying air circulation frozen material | 12/17 12:16:09 |
567 | $B%a%,%X%k%DD62;GH$K$h$k>J%(%M%k%.!<7?4%AgK!$N3+H/(B | 4-h | drying ultrasonic wave particle | 12/21 07:43:53 |
dual-sonic (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-m (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
124 | $B%G%e%"%k%=%K%C%/7?:.9g4o$rMQ$$$FD4@=$7$?HyN3(BAP$B$NN3;RFC@-(B | 12-m | ammonium perchlorate freeze-drying dual-sonic | 12/17 10:32:42 |
dual-stage flow reactor (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
188 | $B%5%$%:!&J,I[$N@)8f$K8~$1$?FsCJ%U%m! | 8-e | Hydrothermal synthesis cerium oxide dual-stage flow reactor | 12/18 14:36:10 |
DWDC (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
228 | An Effective Method for Deriving Asymmetrical Temperature Control Schemes for Dividing-Wall Distillation Columns | 6-d | Asymmetric temperature control DWDC Temperature difference | 12/18 17:39:50 |
dynamic filtration (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
805 | $B@\@~J.N.7?2sE>%I%i%`%U%#%k%?!<$K$h$k9b8zN(_I2a%W%m%;%9$N3+H/(B | 4-b | dynamic filtration tangential flow rotary drum filter | 12/22 23:56:55 |
dynamic fluctuation of CO2 (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
68 | CO2$B$N%a%?%s2=$K$*$1$k(BCO2$BN.NL$NF0E*JQF0$N1F6A(B | 13-g | CO2 Methanation Heterogeneous Catalyst dynamic fluctuation of CO2 | 12/9 09:30:47 |