$B:G=*99?7F|;~!'(B2020-09-26 15:59:01
Machine Learning (8$B7o(B) | ||||
---|---|---|---|---|
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-d (2$B7o(B), 6-e (2$B7o(B), 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
117 | $B%Y%$%::GE,2=$K4p$E$/%(%A%l%s%*%-%7%I@=B$%W%m%;%9$N@_7W(B | 6-b | process design machine learning Bayesian optimization | 12/16 17:50:08 |
136 | $B%Y%$%::GE,2=$K4p$E$/E,1~7?%=%U%H%;%s%5! | 6-d | soft sensor model selection machine learning | 12/17 15:38:03 |
157 | $B5!3#3X=,$r3hMQ$7$?%]%j%^!<%V%l%s%I:`$N3+H/(B | 6-d | Machine learning Polymer composite | 12/17 18:51:12 |
378 | Numerical investigation of optimal control of SiC crystal growth in the RF-TSSG system using machine learning | 6-e | TSSG machine learning magnetic field | 12/20 10:25:45 |
386 | $B5!3#3X=,$rMQ$$$?9b3h@-?(G^$N3+H/(B | 6-e | Machine Learning Catalyst Organic Synthesis | 12/20 11:21:16 |
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 |
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 |
620 | $BB?4DK'9aB2C:2=?eAG$N@\?(J,2rH?1~$X$N5!3#3X=,$NE,MQ(B | 5-a | machine learning feature engineering catalytic cracking | 12/21 18:04:06 |
macropore size (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B IS-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
500 | Effect of Macropore Size of Silica-Supported Cellulose Nanofiber and Their Enhanced Performance for Protein Adsorption | IS-1 | macropore size CNF adsorption | 12/20 18:41:34 |
Magnesium chloride (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
568 | $B2=3XC_G.$rL\E*$H$7$?1v2=%^%0%M%7%&%`(B/$B%"%s%b%K%"7O$NH?1~@-8~>e(B | 9-b | Thermochemical energy storage Magnesium chloride Ammonia | 12/21 08:48:57 |
Magnesium hydride (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
279 | $B6bB0?eAG2=J*$X$N?eAGN.DL$K$h$kG.6!5k$H?eAGJ|=P@)8f$N%7%_%e%l!<%7%g%s(B | 9-e | Magnesium hydride Hydrogen storage Heat transfer | 12/19 13:07:38 |
418 | Mg$B$N?eAG5[B"FC@-$KBP$9$k6bB0;@2=J*$NHy:Y9=B$$*$h$S?(G^5!9=$N8!F$(B | 9-e | Magnesium hydride Hydrogen storage Catalytic mechanism | 12/20 14:13:07 |
Magnesium Hydroxide (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
237 | $B?e;@2=%^%0%M%7%&%`$rMQ$$$?GQ?eCf$N%U%CAG=|5n5!9=$N2rL@$*$h$SDjNL%b%G%k2=(B | 13-b | Magnesium Hydroxide Fluorine Quantitative model | 12/18 19:18:20 |
magnesium ion secondary battery (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 11-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
533 | $BEE@OK!$rMQ$$$?%^%0%M%7%&%`%$%*%sFs2A(B | 11-a | bismuth magnesium ion secondary battery electrodeposition | 12/20 20:25:23 |
magnetic field (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
378 | Numerical investigation of optimal control of SiC crystal growth in the RF-TSSG system using machine learning | 6-e | TSSG machine learning magnetic field | 12/20 10:25:45 |
magnetic nanoparticles (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
298 | $B:YK&Fb4Q;!$X8~$1$?7V8w<'@-J#9gN3;R$NJ,;6!&6E=8@)8f(B | 12-c | magnetic nanoparticles fluorescence dispersibility | 12/19 14:11:28 |
Magnetic Stirrer (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
8 | $B%J%9%U%i%9%3MQ(BHB$BMc7?%9%?!<%i!<$N3+H/(B | 2-b | Mixing Magnetic Stirrer New Type Impeller | 11/19 10:26:25 |
Magnetorheological fluid (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
672 | MR$BN.BN$N$;$sCGN.$l>lCf$K$*$1$kB?N3;R7OD>@\?tCM%7%_%e%l!<%7%g%s(B | 2-e | Magnetorheological fluid Shear flow Apparent viscosity | 12/22 10:14:44 |
Maintenance (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
218 | [$B>7BT9V1i(B] $BJ.L84%AgAuCV$H=D7?9bB.2sE>5!3#(B | SP-9 | atomizer Maintenance spray dryer | 12/18 16:42:49 |
Mammalian cell culture (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
295 | $B%b%N%/%m!<%J%k93BN@=B$$K$*$1$kG]M\J}<0A*Br$N$?$a$N%W%m%;%9%7%_%e%l!<%7%g%s(B | 7-a | Simulation Mammalian cell culture Biopharmaceuticals | 12/19 13:57:23 |
marine biomass (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
69 | $B?eG.=hM}$K$h$kBg7?AtN`$+$i$N%P%$%*%*%$%k@8@.(B | 8-f | marine biomass bio-oil subcritical water | 12/9 10:32:39 |
Markov chain Monte Carlo (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
197 | $B%2%k?;F)%/%m%^%H%0%i%U%#!<$K$h$kJ,;RNLJ,I[?dDj$NIT3N | 6-f | Markov chain Monte Carlo Gel permeation chromatography Molecular weight estimation | 12/18 15:26:48 |
mass transfer (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
406 | $B= | IS-1 | packed column distillation mass transfer total reflux | 12/20 13:46:29 |
671 | Characterization of epoxy-based macro-porous resin in ion-exchange chromatography (Kyoto Inst. Tech.) ($B3X(B)$B!{(BRakotondravao Haingomaholy Michelle$B!&(B | 7-c | ion-exchanger mass transfer separation | 12/22 09:57:56 |
Material Flow Analysis (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B HQ-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
802 | [$B0MMj9V1i(B] $B;:6HO"4X%^%F%j%"%k%U%m!<2r@O$K$h$k@=IJCfBZN1C:AGDjNL2=(B | HQ-21 | Material Flow Analysis Carbon Petrochemical | 12/22 23:51:44 |
Material recycle (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
27 | [$B>7BT9V1i(B] $B%W%i%9%A%C%/%j%5%$%/%k$H%P%$%*%W%i%9%A%C%/(B | SS-1 | Material recycle Chemical recycle Biomassplastics | 12/2 14:39:23 |
Materials Science (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B HC-12 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
603 | [$B=w@->^(B] $B:`NA2J3X$N$?$a$NI=LLNOB,Dj$NE83+(B | HC-12 | Surface Forces Measurement Materials Science Solid-Liquid Interface | 12/21 16:13:29 |
Mathematical model (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$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$N9=C[(B | 9-e | Direct formate fuel cell Mathematical model Fuel transport | 12/21 16:38:34 |
matrix structure (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 11-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
518 | $BC:AGN3;R!&%J%N%A%e!<%VJ#9g<+N)Kl$rMQ$$$?6bB0(BLi$BGvKlFs | 11-a | Li metal anode Carbon nanotubes matrix structure | 12/20 19:27:14 |
MD method (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
809 | MD$B%7%_%e%l!<%7%g%s$rMQ$$$?3$?e1UE)$NJILLIUCe5sF0$HG($l@-$N1vJ,G;EY0MB8@-(B | 12-g | seawater droplets Contact angle MD method | 12/23 00:08:36 |
measurement (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
559 | $B%]%j%V%A%k%a%?%/%j%l!<%H(B+$B%"%k%3!<%kN`$N3H;678?t$NB,Dj$HAj4X(B | 1-a | measurement correlation diffusion coefficient | 12/20 23:49:23 |
mechanical activation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
668 | $B%8%*%]%j%^!<$N9E2=H?1~$K$*$h$\$9%U%i%$%"%C%7%eN3;R$X$N5!3#E*=hM}$N8z2L(B | 13-e | geopolymer mechanical activation Coal fly ash | 12/22 09:31:08 |
mechanism (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
469 | $BD6NW3&?eG.%U%m!<9g@.%7%9%F%`$K$h$k9bG;EY%/%m%`%I!<%W%;%j%"%J%NN3;R$N7A@.5!9=$N2rL@(B | 8-e | supercritical water mechanism nanoparticles | 12/20 17:17:12 |
Mechanochemical reaction (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
175 | $B%a%+%N%1%_%+%kH?1~$rMxMQ$7$?Fq=hM}9[@P$+$i$N4uEZN`2s<}?75,%W%m%;%9$NDs0F(B | 2-f | Mechanochemical reaction Process development Grinding | 12/18 12:53:58 |
medium chain fatty acid (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
519 | $B:?D9$N0[$J$k;iKC;@4p$r;}$D%7%gE|%(%9%F%k9g@.$K$*$1$kH?1~A*Br@-@)8f(B | 5-a | sucrose fatty acid ester medium chain fatty acid porous resin catalyst | 12/20 19:30:14 |
Melt crystallization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$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 |
Membrane (15$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (11$B7o(B), SP-10 (2$B7o(B), SS-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
47 | [$B>7BT9V1i(B] CO2$B2s<}!&M-8zMxMQ$K9W8%$9$k(BDDR$B7?%<%*%i%$%HKl%W%m%;%9$N3+H/(B | SP-10 | CO2 separation membrane | 12/2 17:06:49 |
204 | [$B>7BT9V1i(B] CO2$BJ,N%$N$?$a$NJ,;R%2!<%HKl%b%8%e!<%k$N3+H/(B | SS-8 | pre-combustion membrane CCS | 12/18 16:05:30 |
248 | [$B>7BT9V1i(B] $BKlMxMQE|2=%W%m%;%9$N35MW$H%?%$Z%W%i%s%H$G$N | SP-10 | membrane inhibitor saccharification | 12/19 10:04:53 |
266 | $B%+%k%\%-%7%Y%?%$%s%]%j%^!<$r%0%i%U%H$7$?Dc%U%!%&%j%s%0Kl$N3+H/(B | 4-a | Membrane Low-fouling Carboxybetaine polymer | 12/19 11:16:05 |
345 | FO$B%U%!%&%j%s%0$G$NF)?e5sF0$K5Z$\$9%U%!%&%i%s%HAH@.$N1F6A(B | 4-a | membrane forward osmosis fouling | 12/19 20:27:11 |
359 | [$BM%=(O@J8>^(B] $B8B$i$l$?_I2aB.EY%G!<%?$+$i%U%!%&%j%s%0$N5!9=!&NL$r8DJLH=Dj$9$k;XI8$N3+H/(B | 4-b | filtration fouling membrane | 12/20 09:22:23 |
405 | $BBgNL$N%$%*%s1UBN$r4^M-$9$k9b6/EY%2%kKl$NAO@=$H$=$N(BCO2$BA*BrF)2a@-G=$K4X$9$k8!F$(B | 4-a | Ion gel membrane CO2 separation | 12/20 13:43:29 |
425 | Organic liquid mixture separation using an aliphatic polyketone-based organic solvent reverse osmosis (OSRO) membrane | 4-a | Organic solvent reverse osmosis membrane polyketone | 12/20 14:54:11 |
457 | AEI $B7?%<%*%i%$%HKl$N9g@.J}K!$H$=$NF)2aJ,N%FC@-$N8!F$(B | 4-a | zeolite membrane gas separation | 12/20 16:42:44 |
514 | Influence of catalyst type on water cleaning by photocatalytic membrane contactor (Yamaguchi U.) ($B3X(B)$B!{(BChe Abdul Rahim Azzah Nazihah$B!&(B | 4-a | membrane photocatalyst formic acid | 12/20 19:07:52 |
530 | TiO2-Zeolite $BJ#9gKl$N3+H/(B | 4-a | zeolite membrane catalysis | 12/20 20:15:58 |
569 | $B?e>x5$%9%$!<%W$rMQ$$$?(BCO2$BKlJ,N%%W%m%;%9$K$*$1$k?e>x5$=|5nK!$N1F6A(B | 4-a | CO2 capture membrane separation | 12/21 09:08:16 |
673 | Na-MOR$BKl$rMQ$$$??];@%(%9%F%k9g@.MQ%U%m!<%a%s%V%l%s%j%"%/%?!<$N3+H/(B | 4-a | zeolite membrane membrane reactor | 12/22 10:24:28 |
709 | $B9bJ,;RKl$rMQ$$$?(BCO2$BJ,N%2s<}%W%m%;%9@_7W$H7P:Q@-I>2A(B | 4-a | Separation Membrane Carbon dioxide | 12/22 15:10:55 |
744 | $B9b8zN($N(BCO2$BJ,N%$N$?$a$N@8BNLOJo%^%$%/%m%Q%?!<%s2=Kl(B | 4-a | Membrane CO2 separation Interface | 12/22 18:56:25 |
membrane + distillation hibrid process (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
277 | $B6&J(:.9gJ*J,N%$r | 4-c | membrane + distillation hibrid process azeotropic mixtures ternary azeotrope | 12/19 12:46:19 |
Membrane Bio Reactor (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-10 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
253 | [$B>7BT9V1i(B] MBR($BKlJ,N%3h@-1xE%K!(B)$B$rMxMQ$7$?GS?e=hM}(B ($B;0I)%1%_%+%k%"%/%"!&%=%j%e!<%7%g%s%:(B) ($BK!(B)$B6b;R(B $B??(B | SP-10 | Membrane Bio Reactor Wastewater treatment Hollow fiber membrane | 12/19 10:24:02 |
Membrane bioreactor (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
21 | $BKlJ,N%3h@-1xE%K!$K$*$$$FKlI=LL$N?F?e@-$,%U%!%&%j%s%0$K5Z$\$91F6A(B | 13-b | Membrane bioreactor Membrane fouling Surface hydrophilicity | 11/28 10:45:52 |
Membrane Characterization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
543 | $B?75,$J(BDDS$B%-%c%j%"$r;X8~$7$?(BCubosome$B=89gBN$ND4@=$HI>2A(B | 12-c | Cubosome DDS Membrane Characterization | 12/20 21:29:06 |
Membrane chromatography (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
786 | $B%a%s%V%l%s%/%m%^%H%0%i%U%#!<$K8~$1$?B?=E%b!<%I1~Ez@-9bJ,;R%0%i%U%HKl$N@_7W$HFC@-I>2A(B | 4-a | Membrane chromatography Protein Ion recognition | 12/22 22:42:15 |
Membrane curvature sensing protein (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
446 | $B;i | 7-a | Membrane curvature sensing protein SiO2 particles Proteome analysis | 12/20 16:29:40 |
membrane distillation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
536 | Evaluation of the net effect of the membrane surface structure on the membrane distillation process performance | 4-a | membrane distillation TIPS process | 12/20 20:35:31 |
membrane fluctuation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
727 | $B%?%s%Q%/ | 12-a | liposome membrane fluctuation biosensor | 12/22 16:55:43 |
membrane formation mechanism (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
121 | $B?eG.K!$rMQ$$$?%,%9J,N%MQ%"%b%k%U%!%9%+!<%\%sKl$N:n@=$HI>2A(B | 4-a | Carbon membrane gas separation membrane formation mechanism | 12/16 18:58:56 |
Membrane fouling (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
21 | $BKlJ,N%3h@-1xE%K!$K$*$$$FKlI=LL$N?F?e@-$,%U%!%&%j%s%0$K5Z$\$91F6A(B | 13-b | Membrane bioreactor Membrane fouling Surface hydrophilicity | 11/28 10:45:52 |
Membrane permeation mechanism (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
51 | $B%<%*%i%$%HKl$X$N5$BN$N5[Ce$r9MN8$7$?KlF)2a5!9=$N2r@O(B | 4-a | Membrane permeation mechanism Adsorption Zeolite membrane | 12/3 14:23:34 |
membrane preparation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
767 | Preparation and protein separation application of cibacron blue-modified electrospun PVA membrane | 4-a | membrane preparation protein separation nanofiber membrane | 12/22 21:21:23 |
membrane reactor (4$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-d (2$B7o(B), 4-a (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
366 | $B?eAG%-%c%j%"$H$7$F$N%"%s%b%K%"$NJ,2r%7%9%F%`(B | 5-d | ammonia membrane reactor palladium membrane | 12/20 09:58:24 |
484 | Pd$BKlH?1~4o$rMQ$$$?%a%?%s%I%i%$%j%U%)!<%_%s%0H?1~$X$N1~MQ$rL\;X$7$??(G^3+H/(B | 5-d | membrane reactor oxygen storage capacity catalyst | 12/20 17:58:12 |
618 | CO2$B$r86NA$H$7$?%a%?%N!<%k9g@.$X$NKlH?1~4o$NE,MQ(B | 4-a | membrane reactor methanol process zeolite membrane | 12/21 17:46:29 |
673 | Na-MOR$BKl$rMQ$$$??];@%(%9%F%k9g@.MQ%U%m!<%a%s%V%l%s%j%"%/%?!<$N3+H/(B | 4-a | zeolite membrane membrane reactor | 12/22 10:24:28 |
Membrane separation (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (3$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
348 | $B%7%j%+Cf6u;e$+$i(BCHA$B7?%<%*%i%$%H$X$N7k>=2=@)8f$H(BCO2$BJ,N%$X$N1~MQ(B | 4-a | CHA-type zeolite membrane separation carbon dioxide | 12/19 21:03:20 |
449 | $B3&LL3h@-:^E:2C%"%k%+%j=hM}K!$,(BSilicalite-1$BKl$NF)2aJ,N%FC@-$K5Z$\$91F6A(B | 4-a | Zeolite membrane separation post treatment | 12/20 16:36:23 |
504 | $B%P%$%*%V%?%N!<%kH/9Z$X$NL55!B?9& | 4-a | Membrane separation Butanol Dehydration | 12/20 18:51:38 |
membrane surface modification (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
151 | $B@EEE5[Ce$K$h$kN>@-%$%*%s%3%]%j%^!<$NF3F~$K$h$kKl$NBQ%U%!%&%j%s%0@-$N8~>e(B | 4-a | zwitterionic antifouling membrane surface modification | 12/17 17:50:23 |
meropenem (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
642 | $BJ,;R%$%s%W%j%s%H9bJ,;R8GDj%0%i%U%!%$%H%Z!<%9%HEE6K$rMQ$$$?%a%m%Z%M%`%;%s%5$N:GE,2M66@-%b%N%^! | 7-e | meropenem molecularly imprinted polymer sensor | 12/21 21:54:47 |
Mesenchymal Stem Cell (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
371 | $B:YK&7ABV2r@O$K$*$1$kIJ | 7-a | Mesenchymal Stem Cell image analysis | 12/20 10:04:11 |
mesopores (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
260 | $B<+F0 | 5-a | Automobile catalyst mesopores Effective diffusivity | 12/19 10:58:41 |
mesoporous (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
96 | $B%a%=%]!<%i%9%7%j%+J#9g%2%kEE2rZ(B | 12-a | mesoporous battery | 12/13 19:47:05 |
mesoporous carbon (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-k (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
557 | ZnO$BCr7?%+!<%\%s$N:Y9&9=B$$K4X$9$k8&5f(B | 12-k | mesoporous carbon solvent-free ZnO | 12/20 22:57:12 |
mesoporous silica (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
147 | $BD6NW3&(BCO2$BCf$K$*$1$k%a%=%]!<%i%9%7%j%+$X$N(BVOC$B5[CeJ?9U$NB,Dj5Z$S%b%G%j%s%0(B | 8-c | supercritical carbon dioxide mesoporous silica adsorption | 12/17 16:58:05 |
Metabolic engineering (4$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (4$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
421 | $BBgD26]$rMQ$$$?%a%P%m%s;@@8;:5;=Q$N3+H/(B | 7-a | Escherichia coli mevalonate metabolic engineering | 12/20 14:37:30 |
423 | $B%3%j%M6]$K$*$1$k%7%-%_;@7PO)$N6/2=(B | 7-a | Corynebacterium glutamicum Shikimate Metabolic Engineering | 12/20 14:50:39 |
427 | $BJ,Nv9ZJl$NBe | 7-a | Schizosaccharomyces pombe beta-carotene Metabolic Engineering | 12/20 15:02:21 |
436 | "Parallel Metabolic Pathway Engineering" of Escherichia coli for Shikimate Pathway Derivative Production from Glucose-Xylose Co-substrate | 7-a | Metabolic engineering Escherichia coli Shikimate pathway | 12/20 15:36:08 |
metal extraction (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
240 | 3$B | 4-f | New extraction reagent different frameworks metal extraction | 12/18 20:36:47 |
metal ion (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
801 | $B%$%*%s@-9bJ,;R%2%k$rMQ$$$?6bB0%$%*%s$N7OE}J,N%2s<}(B | 12-e | hydrogel metal ion systematic separation | 12/22 23:48:42 |
Metal nanoparticle (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
232 | $B5$1U%9%i%0N.Fb$G$NJ|EE%W%i%:%^%W%m%;%9$K$h$k6bB0%J%NN3;R$NO"B39g@.(B | 5-c | Metal nanoparticle Plasma process Slug flow | 12/18 17:48:26 |
metal nanoparticles (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
306 | $B%=%k%\%5!<%^%kK!$rMQ$$$?(BRu$B6bB04^M-(BTiO2$B5e>uB?9&BN$N0lCJ3,9g@.(B | 8-e | solvothermal method metal nanoparticles catalytic performance | 12/19 14:50:18 |
Metal Organic Framework (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
282 | $BB?9&@-%J%N7k>=$KJq@]$5$l$?M-5!J,;R$NH/8w@)8f(B | 12-d | nano-sized effect metal organic framework host-guest interaction | 12/19 13:16:37 |
635 | $B%"%k%_%JB?9& | 4-a | MIL-160 Metal Organic Framework Xylene isomers separation | 12/21 19:50:08 |
Metal Organics (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
734 | Cu(tmhd)2$B$N9b29D6NW3&(BH2/CO2$B:.9gN.BNCf$K$*$1$k3H;678?t$NI>2A(B | 8-d | Diffusivity Metal Organics Supercritical H2/CO2 Mixture | 12/22 18:11:34 |
Metal oxides (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
692 | $B6bB0;@2=J*$rMQ$$$??eAG%(%M%k%.! | 9-e | Hydrogen storage Metal oxides Steam electrolysis | 12/22 13:20:32 |
Metal Phosphides (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
335 | Noble Metal- Transition Metal Phosphide Catalysts for Alkaline Water Electrolysis: Oxygen Evolution Reaction | 9-a | Oxygen Evolution Reaction Electrocatalysts Metal Phosphides | 12/19 18:42:15 |
Metal Surface (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SS-2 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
180 | [$B>7BT9V1i(B] $B%J%U%5G.J,2rCf$N6bB0I=LL>e%3!<%/@O=P5sF02r@O(B | SS-2 | Coke Naphtha Metal Surface | 12/18 13:16:28 |
Metal-organic framework (6$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-d (3$B7o(B), HQ-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
259 | [$B0MMj9V1i(B] $BB?9&@-G[0L:xBNN3;R$N0eLtJ,Ln$X$N1~MQ2DG=@-(B | HQ-21 | Metal-organic framework Porous coordination polymer Drug carrier | 12/19 10:50:50 |
313 | $B0!1t7O6bB0M-5!9=B$BN$N(BCO2$B5[CeFC@-$K$*$1$k%[%&AG2M668z2L(B | 12-d | metal-organic framework boron CO2 adsortion | 12/19 15:31:39 |
321 | $B%[%&AG2M66$rM-$9$kF<7O6bB0M-5!9=B$BN$N9g@.$H%,%95[CeI>2A(B | 12-d | metal-organic framework copper CO2 adsorption | 12/19 16:50:52 |
327 | $B6bB0M-5!9=B$BN$NG.J*@-$K$*$1$k7k>=%5%$%:0MB8@-(B | 12-d | metal-organic framework size effect thermal property | 12/19 17:27:08 |
703 | $BB?9&@-G[0L9bJ,;R(BHKUST-1 $B$N7k>=@.D92aDx$NB.EYO@E*2r@O(B | 12-g | Metal-organic framework Nucleation | 12/22 14:43:29 |
788 | $B%=%U%HB?9&@-:xBN$N@.7A2C9)$H%2!<%H5[Ce5sF0$N4KK}2=(B | 12-a | metal-organic framework gate adsorption external force | 12/22 22:48:33 |
metal-organic frameworks (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
397 | [$B>7BT9V1i(B] Investigation of the Metal-Organic Framework/Polyimide Construction via Molecular Simulation | K-2 | Mixed matrix membranes metal-organic frameworks molecular simulation | 12/20 12:38:17 |
789 | $BB?9&@-G[0L:xBNHyN3;R$N5e>u=8@Q9=B$$N:n@=$H5[CeFC@-I>2A(B | 12-a | Metal-organic frameworks Hierarchical structures Microfluidic device | 12/22 23:12:56 |
Metallic ion (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
227 | $B%$%*%s1UBN$+$iD4@=$5$l$k%;%k%m!<%9!&%-%H%5%sJ#9g%2%k$K$h$k6bB05[Ce(B | 4-e | Adsorption Metallic ion Ionic liquid | 12/18 17:31:27 |
methanation (8$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (5$B7o(B), 9-c (2$B7o(B), 5-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
62 | $B%+!<%\%s=[4D%a%?%s2=%7%9%F%`(B $B!=%i%\%9%1!<%k;n835!$rMQ$$$?=[4D%3%s%;%W%H$NZ!=(B | 13-g | CO2 CCU Methanation | 12/6 09:39:59 |
63 | $B%+!<%\%s=[4D%a%?%s2=%7%9%F%`(B -H2$B%9%$!<%W!$%a%?%s2=H?1~G.MxMQ$K$h$k(BCO2$B2s<}F0NO$NDc8:(B- | 13-g | CCU Adsorption Methanation | 12/6 13:44:46 |
65 | $B%+!<%\%s=[4D%a%?%s2=%7%9%F%`!!!=(B $BG.<+N)7?FsCJ%a%?%s2=H?1~4o$N@-G=(B $B!=(B | 13-g | CCU Methanation Heat Recovery | 12/6 18:15:50 |
441 | CO2$B%a%?%s2=H?1~$K$*$1$k?(G^3h@-@)8f$K4p$E$$$?H/G.%^%M!<%8%a%s%H(B | 9-c | methanation CO2 utilization thermal management | 12/20 15:57:26 |
460 | $BB?4I<0%7%'%k%"%s%I%A%e!<%V%a%?%M!<%7%g%sH?1~4o$NEAG.!&H?1~!&N.F0?tCM2r@O(B | 9-c | simulation methanation | 12/20 16:56:07 |
588 | $BH?1~!&EAG.!&N.F0$r9MN8$7$??75,%a%?%M!<%7%g%sH?1~AuCV2r@O%=%k%P!<$N3+H/(B | 5-e | methanation simulation OpenFOAM | 12/21 14:25:50 |
675 | Carbon dioxide methanation in calcium looping process using proton conducting oxides | 13-g | CCU Ca looping Methanation | 12/22 10:44:50 |
681 | $BC:;@1v%k!<%WK!$K$h$kFs;@2=C:AGMxMQ$r;X8~$7$?%+%j%&%`7O%-%c%j%"N3;R$N3+H/(B | 13-g | Methanation CCU Carbonate looping | 12/22 12:31:17 |
Methane decomposition (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
605 | $B2=3X%k!<%WK!$K$h$kE4%I!<%W%P%j%&%`%8%k%3%M!<%H$rMQ$$$?%a%?%sG.J,2r7??eAG@8@.(B | 9-c | Methane decomposition CO2 activation Chemical looping | 12/21 16:14:52 |
Methane hydrate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$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 |
methane partial oxidation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
293 | $B%<%*%i%$%HC4;}(BRh$B?(G^$*$h$S(BCO$B$rMQ$$$?%a%?%s$+$i(BC1$B!"(BC2$B4^;@AG2=9gJ*$X$NE>49H?1~(B | 5-a | methane partial oxidation zeolite Rh catalyst | 12/19 13:55:52 |
methane reforming (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
491 | CeO2$B%J%NN3;R$rMQ$$$?%1%_%+%k%k!<%T%s%07?%a%?%s2~ | 5-a | methane reforming CeO2 nanoparticles Reaction analysis | 12/20 18:27:19 |
methane to methanol (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
145 | Direct conversion of methane to methanol over Copper-Exchanged Zeolite under mild conditions | 5-a | methane to methanol copper-exchanged zeolite reaction process | 12/17 16:54:44 |
Methanol (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$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 |
methanol process (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
618 | CO2$B$r86NA$H$7$?%a%?%N!<%k9g@.$X$NKlH?1~4o$NE,MQ(B | 4-a | membrane reactor methanol process zeolite membrane | 12/21 17:46:29 |
method of measuring (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
524 | $BLZ | 9-f | tar woody biomass method of measuring | 12/20 19:50:14 |
methyl methacrylate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
48 | Measurement and correlation of nitrogen and oxygen solubility in methyl methacrylate (MMA) at (293-313) K | 1-a | methyl methacrylate Gas solubility Experimental data | 12/2 18:00:00 |
methylammonium lead iodide (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-h (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
614 | $B%h%&2=1t%a%A%k%"%s%b%K%&%`%Z%m%V%9%+%$%HKl$N(BCVD$B%W%m%;%9$N3+H/(B | 5-h | CVD methylammonium lead iodide lead melt | 12/21 17:01:52 |
Methylcyclohexane (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 6-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
12 | $B%O%$%7%j%+%<%*%i%$%H$G$N%a%A%k%7%/%m%X%-%5%s0[@-BN$N5[Ce5sF0(B | 4-e | silicalite-1 methylcyclohexane molecular sieve | 11/23 20:08:57 |
590 | $B?eAG6!5kJQF02<$K$*$1$k%H%k%(%s?eAG2=%W%m%;%9$N:GE,2= | 6-c | Renewable energy Methylcyclohexane Toluene hydrogenation | 12/21 14:49:42 |
mevalonate (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
421 | $BBgD26]$rMQ$$$?%a%P%m%s;@@8;:5;=Q$N3+H/(B | 7-a | Escherichia coli mevalonate metabolic engineering | 12/20 14:37:30 |
492 | $B%;%k%m!<%97O%P%$%*%^%9$+$i$N%a%P%m%s;@$N@8;:$r;X8~$7$?BgD26]$NAO@8(B | 7-a | Escherichia coli mevalonate cellulose | 12/20 18:30:05 |