$B:G=*99?7F|;~!'(B2016-01-20 13:09:01
Mab (2$B7o(B) | ||||
---|---|---|---|---|
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-4 (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
952 | $B%"%U%#%K%F%#%/%m%^%H%0%i%U%#!<$K$*$1$k93BNM3Mh6E=8J*$NMO=P5sF0(B | SE-4 | protein A Mab chromatography | 6/19 23:38:42 |
954 | $B?75,93BN@:@=MQ%/%m%^%H%0%i%U%#!<= | SE-4 | packing media Mab chromatography | 6/19 23:44:03 |
macroporous supports (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
574 | $BKlJ,N%MQ%^%/%m%]!<%i%9Hs>= | SY-20 | macroporous supports amorphous silica membrane separator | 6/19 10:10:42 |
Magnesium aluminate spinel (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
34 | [$BM%=(O@J8>^(B] Ni$BCV49(BMgAl2O4$B%9%T%M%kJ#9g;@2=J*$rMQ$$$??75,C:2=?eAG2~ | SY-8 | Magnesium aluminate spinel Nickel catalyst Hydrocarbon reforming | 5/26 11:06:25 |
magnesium carbonate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
786 | $B7Z>F(Bdolomite$B7|By1U$NC:;@2=H?1~$K$h$k(BMg$BC:;@1v$N>=@O$HJ,N%(B | SY-14 | dolomite carbonation magnesium carbonate | 6/19 17:47:20 |
Magnetic particle (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-19 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
698 | $B<'@-2s<}2DG=$J@5?;F)6nF0MO1U$N3+H/(B | SY-19 | FO process Draw solution Magnetic particle | 6/19 15:15:11 |
magnetic responsivity (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
348 | $BC1J,;6%]%j%^!<>.N3;R$X$N<'>l1~Ez@-IUM?$N$?$a$N%X%F%m6E=8$H%7%j%+HoJ$(B | SE-16 | silica-coating heterocoagulation magnetic responsivity | 6/17 17:28:34 |
magnetite (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-17 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
611 | $B<'@-%J%NN3;R$rFbJq$7$?4629@-%2%kHyN3;R$N:n@=(B | SE-17 | thermosensitive hydrogel nanoparticle magnetite | 6/19 11:47:26 |
Maillard reaction model (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-22 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
281 | $BD9%M%.!&%-%c%Y%D4%Ag9)DxCf$N%a%$%i!<%IH?1~$NB.EYO@E*@_7W(B | SY-22 | Maillard reaction model Consecutive Reaction Model Dehydration Response Curves | 6/16 23:47:03 |
Maintenance (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-24 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
914 | $B2=3X;:6H$K$*$1$kJ]29:`2 | SE-24 | CUI Maintenance Corrosion test | 6/19 21:51:30 |
Mammalian-Cell-Culture (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
106 | $B?6$H$&J}<0F0J*:YK&G]M\Ae$N(BCFD$B2r@O(B | SE-14 | Mammalian-Cell-Culture CFD Shaking Stirrer | 6/9 09:32:25 |
Management (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-5 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
215 | $B%W%i%s%H(BEPC$B$K1w$1$k0BA4!&IJ | SY-6 | management Safety cost quality control cost | 6/14 17:43:24 |
559 | [$BE8K>9V1i(B] $B3$30%W%m%8%'%/%H!&%^%M%8%a%s%H$K$*$1$k%7%9%F%`%:!&%"%W%m!<%A!AM}O@!&5;=Q!&E8K>!A(B | SY-5 | Project Management Risk | 6/19 09:19:58 |
manganese peroxidase (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
428 | $BGr?'Ie5`6]$K$h$k%^%s%,%s%Z%k%*%-%7%@!<%<@8;:$K5Z$\$9(BpH$B%7%U%H$N1F6A(B | SE-1 | manganese peroxidase pH white rot fungus | 6/18 13:58:10 |
mannitol (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
515 | Decomposition kinetics of mannose, mannitol and mannuronic acid under hydrothermal condition | SE-7 | mannose mannitol biomass | 6/18 20:42:57 |
mannose (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
515 | Decomposition kinetics of mannose, mannitol and mannuronic acid under hydrothermal condition | SE-7 | mannose mannitol biomass | 6/18 20:42:57 |
Marangoni convection (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-22 (2$B7o(B), SE-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
197 | $B29EY:9(BMarangoni$BBPN.$r9MN8$7$?(BS-CLSVOF$BK!$N3+H/$H8!>Z(B | SE-22 | Marangoni convection VOF S-CLSVOF | 6/13 11:58:50 |
464 | Numerical investigation of the effect of the liquid film volume on thermocapillary flow in a thin circular liquid film ~ various Prandtl number fluids ~ | SE-22 | Marangoni convection Low Prandtl liquid film Volume ratio | 6/18 17:41:27 |
617 | $B29EY:9$HG;EY:9$K5/0x$9$k%^%i%s%4%KBPN.$N6&B88z2L$K$h$kBPN.9=B$0MB8@-$K4X$9$k?tCM2r@O(B | SE-11 | Marangoni convection Floating zone technique Si/Ge | 6/19 11:56:30 |
Marangoni effect (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
723 | $BHy:YN.O)Fb$N5$1U<+M33&LL>e$KM65/$7$?%^%i%s%4%KBPN.$N2D;k2=$H$=$NB.EY7WB,(B | SE-11 | Marangoni effect PIV Capillary channel | 6/19 16:00:39 |
Marangoni flow (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-12 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
355 | $B<+M3I=LL$NJQ7A$r9MN8$7$?%$%s%/%8%'%C%H1UE)$NGvKl7A@.2aDx$N?tCM2r@O(B | SE-12 | Marangoni flow drying Inkjet print | 6/17 18:48:58 |
marine green alga (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
268 | $B%?%^%M%.30Hi$*$h$S3$;:NPAt%"%J%"%*%5$K$h$k=E6bB0%$%*%s$N5[CeJ,N%(B | SE-20 | biosorption onion skin marine green alga | 6/16 17:15:25 |
Mass Transfer (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
703 | $B%9%i%0%U%m!<$rMQ$$$?5$1U8GH?1~%W%m%;%9$N6/2=(B | SY-3 | slug flow catalyst mass transfer | 6/19 15:20:24 |
957 | $B%9%i%0N.$K$*$1$kAj4VJ* | SY-10 | Slug flow Mass Transfer Computational Fluid Dynamics | 6/19 23:56:43 |
983 | [$B0MMj9V1i(B] PEFC$BB?9& | SP-3 | PEFC catalyst layer mass transfer | 6/26 19:37:20 |
mass transfer coefficient (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-18 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
620 | Mass transfer coefficient of organic solvent in supercritical carbon dioxide drying | SE-18 | supercritical carbon dioxide drying mass transfer coefficient | 6/19 12:05:14 |
738 | $B%9%Q%$%i%k4I$rMQ$$$k5[<}<0%R!<%H%]%s%W$N5[<}1UKlG.!&J* | SE-22 | Absorption heat pumps Lithium bromide Mass transfer coefficient | 6/19 16:36:52 |
mass transfer model (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
14 | $B= | SY-3 | Packed distillation column ideal plate model mass transfer model | 5/18 17:01:34 |
Mass transport (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
770 | $BD>@\%.;@7AG3NAEECS$NJ* | SY-21 | Direct formic acid fuel cell Mass transport Crossover | 6/19 17:27:08 |
matching between processes (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-4 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
891 | $BB?IJ | SY-4 | matching between processes entropy scheduling | 6/19 20:57:52 |
Maxblend (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
334 | $BHs%K%e!<%H%sN.BNCf$K$*$1$kBg7?Mc$HB?CJMc$N:.9gFC@-$NHf3S(B | SE-14 | Power Consumption Mixing time Maxblend | 6/17 15:52:57 |
maximum entropy method (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-21 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
743 | $B%"%k%*!<%I@P7?N2;@E4%J%H%j%&%`$K$*$1$k9bB.%$%*%s3H;6%a%+%K%:%`$N2rL@(B | SY-21 | rechargeable battery neutron diffraction maximum entropy method | 6/19 16:48:01 |
Maxwell-Stefan equation (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-13 (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
421 | $B9bN3;RG;EY%9%i%j! | SY-13 | Slurry coating Maxwell-Stefan equation Drying model | 6/18 13:27:11 |
425 | $B9bN3;RG;EY%9%i%j! | SY-13 | Slurry coating drying Maxwell-Stefan equation Polymer layer formation | 6/18 13:40:22 |
MEA (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
393 | MEA$B$rMQ$$$?(BCO2$BJ,N%2s<}$N:F@8Ec$K$*$1$k(BCO2$B2rN%G.$NDjNL2=(B | SY-11 | CO2 capture MEA heat of CO2 dissociation | 6/18 11:27:37 |
measurement (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-18 (2$B7o(B), SE-13 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
664 | [$BE8K>9V1i(B] $B:.9g7OG.G^BN$N(BHelmholtz$B4X?t7?>uBVJ}Dx<0$N9b@:EY2=(B | SE-18 | Equation of State Measurement Working Fluid | 6/19 14:00:22 |
780 | $B%;%_%/%i%9%l!<%H@8@.7O(B(Nitrogen + Tetra-n-butylammonium Bromide + Water)$B$K$*$1$kCbAG%,%9$NMO2rEYB,Dj(B | SE-18 | Tetra-n-butylammonium Bromide solubility measurement | 6/19 17:35:40 |
958 | $B5$CfHyN3;R$N0[AG:`I=LL$X$ND@CeNL7WB,%7%9%F%`$N9=C[(B | SE-13 | aerosol deposition measurement | 6/19 23:57:54 |
Mechano-chemical method (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
262 | $B%a%+%N%1%_%+%kK!$K$h$jD4@=$7$?J#9g?e;@2=J*$NC&?e?eOB5sF0(B | SE-8 | Chemical heat storage Mechano-chemical method Hydroxide composite | 6/16 16:12:31 |
mechanochemical (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-17 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
843 | $B%a%+%N%1%_%+%kK!$K$h$k%<%*%i%$%H7?:xBN7k>=$N9g@.(B | SE-17 | zeolitic imidazolate frameworks mechanochemical adsorption | 6/19 19:19:16 |
Mechanochemical processing (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-13 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
529 | $BM7@17?%\!<%k%_%k$rMQ$$$?;@2=J*J#9g2=%W%m%;%9$H%<%*%i%$%H9g@.$X$N1~MQ(B | SE-13 | Mechanochemical processing Composite formation Zeolite crystallization | 6/18 21:31:05 |
mechanochemical synthesis (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-13 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
122 | $B6bB0?e;@2=J*$NMO2rEY@Q$r9MN8$7$?E47OAX>uJ#?e;@2=J*$N%a%+%N%1%_%+%k9g@.(B | SE-13 | layered double hydroxide mechanochemical synthesis ball-milling | 6/10 17:33:05 |
Medical device (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
610 | [$B>7BT9V1i(B] $B0eNE5!4o3+H/$H9bJ,;R:`NA(B | SE-3 | Medical device Polymer | 6/19 11:46:47 |
Melt (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
22 | $B?e;@2=%9%H%m%s%A%&%`(B8$B?e1v7k>=$rE:2C$7$?1v2=%+%k%7%&%`(B6$B?e1vM;1U$N2aNd5Q29EY$K5Z$\$9 | SY-14 | Nucleation Melt Heat Storage | 5/21 10:00:13 |
melt crystallization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-14 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
171 | $B;iKC;@$NM;1U>=@O$K$*$1$kMO | SY-14 | melt crystallization effective distribution coefficient solute distribution theory | 6/12 11:37:40 |
membrane (8$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-20 (3$B7o(B), SE-15 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
135 | [$B>7BT9V1i(B] $BB?9&@-J,N%Kl$N3+H/$H%W%m%;%96/2=$X$N1~MQ(B | SY-3 | membrane separation process intensification | 6/11 10:49:34 |
175 | $B002=@.%1%_%+%k%:$NKl$m2a5;=Q>R2p(B | SY-20 | Membrane Clarification | 6/12 12:15:44 |
578 | $B%$%`(B $B%N%/%m%^%H$*$h$S3K;@%/%m%^%H$KE,$7$?%a%s%V%l%sAG:`$N3+H/$H@8BNJ,;R$N8GDj2=(B | SE-1 | Membrane Non-specific adsorption Immuno-Chromatography | 6/19 10:15:09 |
579 | $B%<%*%i%$%HKlJ,N%$NE83+(B | SY-20 | zeolite membrane separation | 6/19 10:15:37 |
580 | $B%(%A%l%s%W%m%;%9$X$NKlJ,N%5;=Q$NE,MQ2DG=@-(B | SY-20 | ethylene production membrane separation | 6/19 10:17:43 |
635 | MFI$B7?%<%*%i%$%HKl$NF)2aJ,N%@-$KM?$($k;Y;}BN:Y9&7B$N1F6A(B | SE-20 | zeolite membrane gas separation | 6/19 12:46:00 |
765 | $B%^%$%/%m%U%k%$%G%#%/%9$HKl5;=Q$rM;9g$7$?%@%V%k%(%^%k%7%g%sD4@=K!$N3+H/(B | SE-16 | microfluidics membrane emulsion | 6/19 17:20:43 |
885 | $BNW3&E@0J2<(B150$B!n$^$G;HMQ2DG=$J%Q%i%8%&%`J#9gKl$N:n@=$H@-G=I>2A(B | SE-15 | Hydrogen Palladium Membrane | 6/19 20:35:22 |
Membrane Bioreactor (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
833 | $BCf6u;eKl$rMQ$$$?(BMBR $B%7%9%F%`$N3+H/$HE,MQ;vNc(B | SY-20 | Membrane Bioreactor Hollow Fiber Membrane Wastewater Treatment | 6/19 19:02:48 |
membrane electrode assembly (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
724 | $BA48GBN%"%k%+%jG3NAEECS$K$*$1$k(BMEA$B$N9=B$@)8f$H@-G=2r@O(B | SE-9 | solid-state alkaline fuel cell membrane electrode assembly | 6/19 16:01:58 |
Membrane fabrication at low temperature (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-19 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
444 | $B%7%k%;%9%-%*%-%5%sKl$N8w%>%k(B-$B%2%k@=Kl$*$h$S$=$NF)2aFC@-(B | SY-19 | Photo-induced polymerization Membrane fabrication at low temperature Inorganic/organic hybrid membrane | 6/18 16:06:29 |
membrane filtration (4$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-18 (3$B7o(B), SY-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
318 | $B%X%j%+%k%P%C%U%kIU$-Cf6u;eKl%b%8%e!<%k$N@-G=$HN.F0>uBV$N4X78(B | SY-3 | CFD Membrane Filtration Process Intensification | 6/17 14:23:01 |
489 | $BJ?HD7?(BMF$BKl$K$*$1$k%1!<%/AX8|$5$N@)8f(B(4) | SY-18 | Membrane Filtration Aeration Flow Flow Rate Distribution | 6/18 18:51:26 |
858 | $B:YK&LOJo%Y%7%/%k$NKl_I2aFC@-$NI>2A(B | SY-18 | membrane filtration vesicle cell | 6/19 19:45:47 |
870 | $B%3%m%$%I$NKl_I2a$K$*$1$k_I2a05NO$N5^JQ$KH<$&KlF)2aN.B+$N2aEOFC@-(B | SY-18 | membrane filtration permeation flux filtration pressure | 6/19 20:08:36 |
membrane fouling (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (2$B7o(B), SY-19 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
495 | $BN>@-%$%*%s@-%^%F%j%"%k$NMOG^OB9=B$$KCeL\$7$?Kl%U%!%&%j%s%05sF0$N7W;;2=3XE*2r@O(B | SY-19 | membrane fouling molecular dynamics solvation structures | 6/18 19:26:21 |
602 | $B%U%!%$%s%P%V%k$NKl%U%!%&%j%s%0M^@)8z2L$KBP$9$k(BQCM-D$BK!$K$h$k2r@O(B | SE-20 | fine bubble membrane fouling QCM-D | 6/19 11:18:48 |
637 | $BDcG;EY$N | SE-20 | membrane fouling chemically enhanced backwash NaClO | 6/19 12:49:52 |
Membrane module (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
638 | $B?;F)05H/EE$K$*$1$k1?E>>r7o$,H/EE8zN($KM?$($k1F6A(B | SE-20 | Pressure retarded osmosis Membrane module Operating condition | 6/19 12:53:07 |
membrane permeation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
727 | $BL}E)$NKl:Y9&F)2a$K4X$9$k?tCM%7%_%e%l!<%7%g%s(B | SE-16 | Lattice Boltzmann method Two-phase flow membrane permeation | 6/19 16:16:17 |
Membrane permeation model (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-19 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
228 | $BHsJ?9UG.NO3X$K4p$E$/@5?;F)F)2a%b%G%k$HMW5aKl@-G=$N8!F$(B | SY-19 | Forward osmosis Membrane permeation model Non-equilibrium thermodynamics | 6/15 17:15:23 |
membrane reactor (5$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-3 (3$B7o(B), SY-19 (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
413 | $B%<%*%i%$%HKl$rMQ$$$?%a%?%N!<%k9g@.%a%s%V%l%s%j%"%/%?!<$N2DG=@-(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B | SY-19 | methanol synthesis membrane reactor ZSM-5 membrane | 6/18 13:08:13 |
615 | $B%7%j%+Kl$rEk:\$7$?KlH?1~4o$rMQ$$$??e@-%,%9%7%U%HH?1~$N8!F$(B | SY-19 | silica membrane membrane reactor water gas shift reaction | 6/19 11:54:03 |
972 | [$B0MMj9V1i(B] $B?eAG%-%c%j%"MxMQ$N$?$a$NKl5;=Q(B | SP-3 | Chemical Hydrogen Carrier Membrane Reactor Hydrogen Separation | 6/26 19:33:05 |
973 | [$B0MMj9V1i(B] $B%Q%i%8%&%`KlJ,N%$rH<$&?eAG@=B$(B | SP-3 | Hydrogen production Membrane reactor Palladium | 6/26 19:33:33 |
988 | [$B0MMj9V1i(B] $B%7%j%+Kl5Z$SKlH?1~4o$K$h$k?eAG@=B$(B | SP-3 | silica membrane membrane reactor hydrogen Production | 6/26 19:39:19 |
Membrane Separation (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
84 | $B29EY1~Ez@-Kl$NJ,;RF)2aFC@-$K5Z$\$92M66:^E:2C$N8z2L(B | SE-19 | PNIPAM Cross-linker Membrane Separation | 6/5 11:59:21 |
838 | $B9b?;F)05$rM-$9$k29EY1~Ez@-%$%*%s1UBN$NAO@=$H@5?;F)K!$X$NE,MQ(B | SE-20 | ionic liquid membrane separation osmotic pressure | 6/19 19:09:48 |
membrane separator (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
574 | $BKlJ,N%MQ%^%/%m%]!<%i%9Hs>= | SY-20 | macroporous supports amorphous silica membrane separator | 6/19 10:10:42 |
membrane structure (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-18 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
868 | $B4uGv%3%m%$%I$N@:L)_I2aFC@-$HKl9=B$$N4X78$N%b%G%j%s%0(B | SY-18 | microfiltration dilute colloids membrane structure | 6/19 20:03:19 |
Membrane synthesis (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-19 (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
475 | $B%]%j%^! ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B | SY-19 | membrane synthesis ZSM-5 polymer | 6/18 18:17:53 |
829 | CHA$B7?%"%k%_%N%j%s;@1v7O%<%*%i%$%HKl$N9g@.$HF)2aJ,N%@-G=(B | SY-19 | Aluminophosphate Membrane synthesis Permeability | 6/19 18:52:29 |
Membrane-electrode-assembly (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
479 | $BD63J;RGr6b9g6b?(G^$rMQ$$$?(BPEFC$BMQ9bBQ5WKlEE6K@\9gBN$N3+H/(B | SE-9 | Superlattice Membrane-electrode-assembly Polymer electrolyte fuel cells | 6/18 18:28:28 |
membranes (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
996 | [$B0MMj9V1i(B] $B | SP-3 | aromatic polymers membranes ion conduction | 6/26 19:42:21 |
Membranome (6$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-1 (2$B7o(B), SE-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
874 | $B<+8JAH?%2=Kl$N%G%6%$%s$K$h$kJ,;RG'<15!G=$N@)8f$*$h$S$=$N1~MQ(B | SE-19 | Membranome Liposome Chiral Recognition | 6/19 20:19:04 |
877 | $B3&LLH?1~>l$H$7$F$N(BAOT$B%Y%7%/%kKl>l%G%6%$%s(B | SE-16 | Membranome AOT Vesicle PADPA | 6/19 20:22:38 |
879 | $B%"%K%*%s5[C&Ce:^$N3+H/$rL\;X$7$?%j%]%=!<%`Kl>l$N@5EE2Y%_%/%m%I%a%$%s$N2r@O(B | SE-17 | Membranome Cationic Liposome Localized Electrostatic Potential | 6/19 20:26:25 |
882 | $B%_%/%m%I%a%$%sKl>l$K$*$1$k%$%V%W%m%U%'%s$N%-%i%kA*BrE*J,G[5sF0(B | SE-20 | Membranome Heterogeneous Liposome Ibuprofen | 6/19 20:30:13 |
884 | $B3K;@J,;R$N9b~%Y%7%/%k$NKl>l%G%6%$%s(B | SE-1 | Membranome Guanidinium-Modified Vesicles Nucleic Acid Recognition | 6/19 20:33:04 |
886 | $BBe | SE-1 | Membranome Caldilipin-Modified Liposome Isocitrate Dehydrogenase | 6/19 20:36:13 |
mercury (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
577 | $B938693BNH?1~$rMxMQ$7$??e6d%$%*%s$N4J0WJ,@O(B | SY-11 | mercury antibody simple analysis | 6/19 10:13:54 |
Mesenchymal stem cell (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
27 | $B4VMU7O44:YK&A}?#MQ$N%^%$%/%m%-%c%j%"$H3IYB>r7o$N8!F$(B | SE-2 | Mesenchymal stem cell microcarrier agitation | 5/22 15:51:11 |
52 | $B4VMU7O44:YK&IuF~%O%$%I%m%2%k$rMQ$$$?J"KlL~CeKI;_8z2L$N8!F$(B | SE-3 | mesenchymal stem cell peritoneal adhesion hydrogel | 6/1 18:11:22 |
mesh size (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-15 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
395 | Pd$BHyN3;R?(G^$N0BDj@-$r8~>e$5$;$k%J%N%2%kC4BN$N@_7W(B | SY-15 | nanogel mesh size Ostwald ripening | 6/18 11:41:41 |
mesoporous carbon (4$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-21 (2$B7o(B), SE-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
195 | $B7k>=@-(BMo-V-O$BJ#9g;@2=J*?(G^$N%b%k%U%)%m%8!<@)8f$H%(%?%s;@2=H?1~$X$N1~MQ(B | SY-8 | selective oxidation catalysts metal oxides mesoporous carbon | 6/12 22:53:39 |
350 | $B:Y9&Fb9g@.$K$h$kHy>.$J&A(B-MnO2$B$H%+!<%\%s%2%k$NJ#9g2=(B | SY-21 | electrode material nano composite mesoporous carbon | 6/17 18:00:24 |
524 | $B?e;@2=%j%A%&%`(B/$B%a%=%]!<%i%9%+!<%\%s$NJ#9g2=$K$h$k?75,2=3XC_G.:`$N8!F$(B | SE-8 | chemical heat storage lithium hydroxide mesoporous carbon | 6/18 21:10:51 |
625 | $B%j%A%&%`6u5$EECS@56K:Y9&9=B$$,(BLi2O2$B@O=PNL$KM?$($k1F6A(B | SY-21 | Lithium-Air battery mesoporous carbon pore structure | 6/19 12:16:58 |
mesoporous silica (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-15 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
290 | $B<<299g@.(BMg$B$*$h$S(BAl$B4^M-(BMCM-41$B$N?(G^:nMQ(B | SE-15 | mesoporous silica base catalyst acid catalyst | 6/17 10:25:22 |
mesoporous silica alumina (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
83 | $B8GBN;@?(G^$K$h$k%P%$%*%*%$%k%b%G%k2=9gJ*$N2~ | SE-7 | bio-oil mesoporous silica alumina upgrading | 6/5 11:39:46 |
mesoporous silica membrane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
648 | $B%a%=%]!<%i%9%7%j%+GvKl7A@.$K$*$1$k:n@=$*$h$SCr7?=|5n>r7o$N1F6A(B | SE-20 | mesoporous silica membrane template removal condition solvent extraction | 6/19 13:20:19 |
Metal Hydride (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SP-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
976 | [$B0MMj9V1i(B] $B?@8M@=9]=j$K$*$1$k?eAG | SP-3 | Hydrogen Metal Hydride Compressor | 6/26 19:34:38 |
metal ion (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
161 | $B9b6/EY$J%"%_%s7OCj=P:^FbJq%(%^%k%7%g%s%2%k$N3+H/(B | SE-17 | emulsion gel adsorption metal ion | 6/12 10:02:30 |
603 | $B%$%*%s@-4629@-%2%k$N6bB0%$%*%s$N5[C&CeFC@-$K41G=4p$,M?$($k1F6A(B | SY-16 | thermosensitive gel adsorption metal ion | 6/19 11:18:50 |
Metal organic framework (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-19 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
649 | $BB?9&@-G[0L9bJ,;R(BUiO-66$BKl$N9g@.$HKlJ,N%$X$N1~MQ(B | SY-19 | Metal organic framework UiO-66 Solvothermal synthesis | 6/19 13:21:53 |
metal oxides (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
195 | $B7k>=@-(BMo-V-O$BJ#9g;@2=J*?(G^$N%b%k%U%)%m%8!<@)8f$H%(%?%s;@2=H?1~$X$N1~MQ(B | SY-8 | selective oxidation catalysts metal oxides mesoporous carbon | 6/12 22:53:39 |
metal precursor (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-5 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
460 | $BD6NW3&(BCO2$BJ70O5$2<$K$*$1$kB?9&@-%7%j%+$X$N?(G^6bB0A06nBN$N5[CeJ?9UB,Dj$H2r@O(B | SE-5 | supercritical impregnation metal precursor adsorption equilibria | 6/18 17:33:14 |
Metal recovery (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-13 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
800 | $BJ4:U$K$h$k | SE-13 | Metal recovery Circuit board Grinding | 6/19 18:02:38 |
801 | $B%3%P%k%H;@%j%A%&%`$N?eG.;@?;=P$K4X$9$k8!F$(B | SE-5 | Recycle Separations Metal recovery | 6/19 18:04:28 |
metal recycling (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
239 | $B%-%l!<%H:^$rMQ$$$?%P%$%]!<%iKlEE5$F)@O$K$h$k6bB0$N%j%5%$%/%k(B | SY-11 | metal recycling bipolar membrane electrodialysis chelating agent | 6/16 09:31:06 |
Metal salts (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
735 | $B | SE-8 | Water vapor sorption Metal salts Anodized alumina | 6/19 16:34:05 |
metal substrate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
265 | $B6bB0;Y;}(BSOFC$B%;%k$N@-G=I>2A(B | SE-9 | Solid Oxide Fuel Cell metal substrate thin film | 6/16 16:41:56 |
metal-metal bonding (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
4 | Cu2O$B%J%NN3;R$N:n@=$H$=$N@\9gFC@-(B | SE-16 | Cuprous oxide low-temperature metal-metal bonding | 5/13 18:20:43 |
metal-organic framework (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-16 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
339 | $BB?9&@-G[0L:xBN$N(BX$B@~9=B$2r@O$K4p$E$/%2!<%H5[Ce5sF0$N7W;;2J3XE*8!F$(B | SE-16 | metal-organic framework gate adsorption free energy analysis | 6/17 16:07:39 |
metallurgical coke (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
726 | $BNt | SE-8 | metallurgical coke gasification kinetics | 6/19 16:14:26 |
metanephros (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-1 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
521 | $B?UB!864p:YK&$rMQ$$$??UAH?%$N:F9=C[(B | SE-1 | metanephros transplantaion RWV | 6/18 21:00:28 |
Methanation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
789 | CO2$B$N%a%?%sJQ49$N$?$a$N(BNi$B7O%O%K%+%`7?9=B$BN?(G^(B | SY-8 | Structured catalyst Methanation Ni-based catalyst | 6/19 17:52:12 |
methane (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-11 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
335 | $B%"%s%b%K%&%`1v6&B82<$K$*$1$k%a%?%s%O%$%I%l!<%H$NAjJ?9U>r7o$NB,Dj(B | SE-18 | hydrate phase equilibrium methane | 6/17 15:53:34 |
709 | $BL}J,$r4^$`M-5!GQ?e$N7y5$=hM}$K$*$1$k%a%?%s@8;:(B | SY-11 | Methane anaerobic treatment fat | 6/19 15:34:49 |
Methane Dry Reforming (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
416 | $BG3NAEECSGSG.M-8zMxMQ$rL\E*$H$7$?%I%i%$%j%U%)!<%_%s%0?(G^$N8&5f(B | SE-9 | Supported Catalyst Methane Dry Reforming Ionic Conductivity | 6/18 13:20:16 |
Methane storage (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-17 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
57 | $B9bL)EY2=$K$h$k%+!<%\%s%2%k$N%a%?%s5[B"FC@-$N8~>e(B | SY-17 | Carbon cryogel Methane storage Sol-gel polycondensation | 6/2 12:53:13 |
methanol oxidation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
387 | $B2=3X5[C&CeK!$rMQ$$$?G3NAEECS?(G^$NFC@-I>2A(B | SE-9 | chemisorption support effect methanol oxidation | 6/18 10:53:14 |
methanol reforming (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-10 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
73 | $B%(%C%A%s%0%"%k%_%K%&%`4SDLKl$rMQ$$$?%^%$%/%m%j%"%/%?$N3+H/(B | SY-10 | microreactor etching methanol reforming | 6/4 14:58:50 |
methanol synthesis (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
149 | $B%$%s%I%M%7%"$KE,9g$7$?Dc%3%9%H%a%?%N!<%k9g@.?(G^(B | SE-8 | methanol synthesis catalyst | 6/11 17:15:32 |
413 | $B%<%*%i%$%HKl$rMQ$$$?%a%?%N!<%k9g@.%a%s%V%l%s%j%"%/%?!<$N2DG=@-(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B | SY-19 | methanol synthesis membrane reactor ZSM-5 membrane | 6/18 13:08:13 |
Methyl levulinate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-7 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
43 | $B8GBN;@?(G^$rMxMQ$7$?E|N`$+$i$N%l%V%j%s;@%a%A%k$N9g@.(B | SE-7 | Methyl levulinate Solid acid catalyst Saccharides | 5/29 20:37:06 |
Methyl methacrylate(MMA) (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
572 | [$B>7BT9V1i(B] $B%a%?%/%j%k;@%a%A%k(B(MMA)$B@=B$%W%m%;%9$N?7E83+(B-$B?7%(%A%l%sK!(B (Alpha$BK!(B)$B$N3+H/(B | SY-8 | Methyl methacrylate(MMA) Alpha process Ethylene | 6/19 10:03:48 |
Methylcyclohexane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-8 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
798 | $B%a%A%k%7%/%m%X%-%5%sC&?eAG$N$?$a$N(BPt/TiO2$B7O9=B$BN?(G^$NFC@-I>2A(B | SY-8 | Organic chemical hydride Methylcyclohexane Pt-based catalyst | 6/19 18:01:30 |
Methylene blue (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-3 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
916 | $BD62;GH>H | SY-3 | Degradation Methylene blue Ultrasound | 6/19 21:59:05 |
methyltrichlorosilane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-9 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
747 | $BD69b%"%9%Z%/%HHf%_%/%m%-%c%S%F%#$rMQ$$$?(BSiC-CVI$BK!$N%b%G%j%s%0(B | SY-9 | CVD SiC methyltrichlorosilane | 6/19 16:57:45 |
MF/UF and RO membrane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SY-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
607 | MF/UF$BKl5Z$S(BRO$BKl0BDj1?E>$K8~$1$?6E=8=hM}$N1F6A(B | SY-20 | MF/UF and RO membrane Coagulation agent Organic substance sensor | 6/19 11:30:25 |
MFI zeolite membrane (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
326 | $B%<%*%i%$%HKl$K$h$k9bB.?];@>x5$G;=L(B | SE-20 | MFI zeolite membrane porous silica substrate acetic acid condensation | 6/17 14:56:16 |
330 | NaF$BE:2C$K$h$k(BMFI$B%<%*%i%$%HKl$NF)2a@-8~>e(B | SY-19 | MFI zeolite membrane porous silica substrate NaF | 6/17 15:22:46 |
MFI-type zeolite (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B SE-20 (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
715 | $B?e>x5$6&B82<$K$*$1$k(BMFI$B7?%<%*%i%$%H$N(BCO2$B5[Ce$KBP$9$k(BCore-Shell$B2=$N8z2L(B | SE-20 | MFI-type zeolite Core-Shell CO2 adsorption | 6/19 15:49:20 |