$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
---|---|---|---|---|---|
$BH?1~9)3X(B | |||||
(9:12$B!A(B10:24) ($B:BD9(B $B?@@.(B $B>09n!&>.Ln(B $BEX(B) | |||||
C02 | $B%-%7%m!<%9?eAG2=H?1~$K$h$k(BC5$BE|%"%k%3!<%kA*Br9g@.$rL\E*$H$7$?C:AGC4;}F(G^$N3+H/(B | Xylose Hydrogenation Carbon supported Cu catalyst | 5-g | 222 | |
C03 | $B%P%$%*%^%9M3Mh$N5!G=@-C:AG?(G^$K$h$k%U%k%/%H!<%9$+$i(B5-hydroxymethylfurfural$B$N9g@.(B | Humic acid oxygen groups ionic liquid | 5-a | 293 | |
C04 | $B%U%k%/%H!<%9$+$i(BEMF$B$X$N%o%s%]%C%HJQ49$r2DG=$K$9$k%a%+%N%1%_%+%kK!$K$h$j9g@.$7$?%"%_%N(B-$B%V%l%s%9%F%C%I;@Fs41G=@-?(G^(B | mechanochemical bifunctional one-pot | 5-a | 297 | |
C05 | $BCf6uC4BN$X$N%i%C%+!<%<@QAX8GDj2=K!$N2~NI$H5!G=I>2A(B | laccase graft polymerization biodegradation | 5-a | 60 | |
C06 | $B%P%$%*%^%9G3NACf$N%+%j%&%`@.J,$N?WB.$JCj=P!&DjNLJ}K!$N3NN)(B | Biomass Potassium Quantification | 5-g | 125 | |
C07 | $BF0?"J*@-L};i$+$i9g@.$5$l$?3&LL3h@-:^$N@v>tNO$K4X$9$k8&5f(B | surfactants detergency CMC | 5-i | 174 | |
$B5Y7F(B | |||||
$BH?1~9)3X(B | |||||
(10:36$B!A(B12:00) ($B:BD9(B $B>.Ln(B $BEX!&%9%_%9(B $B%j%A%c!<%I(B) | |||||
C09 | $BGQ4~J*%,%92=%,%9$+$i$N%8%a%A%k%(!<%F%kD>@\9g@.(B | dimethyl ether (DME) catalysts gasification gas | 5-a | 266 | |
C10 | $B%>%k(B-$B%2%kK!$GD4@=$7$?F<7O%"%k%_%J?(G^$K$h$kFs;@2=C:AG?eAG2=H?1~(B | dimethyl ether (DME) carbon dioxide (CO2) hydrogenation | 5-a | 249 | |
C11 | $B5$AjCf$K$*$1$k%a%A%k%7%/%m%X%-%5%s$+$i$NC&?eAGH?1~%W%m%;%9$N:GE,2=(B | Dehydrogenation Heat balance analysis Methylcyclohexane | 5-a | 57 | |
C12 | Ni$BC4;}%O%$%I%m%-%7%"%Q%?%$%H?(G^$rMQ$$$?%P%$%*%^%9%?!<%kDc29J,2r3h@-(B | hydroxyapataite nickel biomass tar | 5-a | 110 | |
C13 | $B%$%=%V%?%N!<%k$+$i$N(Bp-$B%-%7%l%sA*Br9g@.$r;X8~$7$?(BZn$BC4;}(BZSM-5$B?(G^$N3+H/(B | Isobutanol Zn loaded ZSM-5 p-Xylene | 5-a | 230 | |
C14 | $B%W%m%H%s%?%$%W(BY$B7?%<%*%i%$%H$rMQ$$$?0BA4$J%(%9%F%k2=$N3NN)(B | esterification H⁺Yzeolite acid catalyst | 5-a | 172 | |
C15 | $B9b9;2=3X$G3X=,$9$kJ* | phenol one-step synthesis palladium | 5-a | 239 | |
$BCk5Y$_(B | |||||
$BH?1~9)3X(B | |||||
(13:00$B!A(B14:24) ($B:BD9(B $B:4F#(B $BOB9%!&Ip@P(B $B70(B) | |||||
C21 | CO2$B?eAG2=$+$i$N%a%?%N!<%k9g@.MQ(BLa$BE:2C(BZnZrOx$B?(G^$N3+H/(B | CO2 hydrogenation Metal Oxide Catalysts Zn | 5-a | 163 | |
C22 | CO2$B?eAG2=H?1~MQ%?%s%G%`7??(G^$K$h$kDc5i%*%l%U%#%s9g@.(B | CO2 hydrogenation Zeolite Lower olefin | 5-a | 166 | |
C23 | $BG3NAEECS$N8GBN9bJ,;RKl$N?eAGF)2aN.B+(B | Polymer electrolyte fuel cell Hydrogen crossover Gas chromatography | 5-a | 168 | |
C24 | $BD62;GH>H | uitrasound cavitation dissolution | 5-b | 271 | |
C25 | $BD62;GH$NJ*M}:nMQ$K5Z$\$91UCf$NMOB85$BNG;EY$N1F6A(B | ultrasound cavitation erosion | 5-b | 272 | |
C26 | $B%^%$%/%mGH>H | Biodiesel Global warming Glycerin | 5-g | 103 | |
C27 | $B%k%_%N!<%kH?1~$N>HEY$H;~4VH/8w$K4X$9$k8&5f(B | luminol catalyst potassium ferricyanide | 5-a | 270 | |
$B5Y7F(B | |||||
$BH?1~9)3X(B | |||||
(14:36$B!A(B15:48) ($B:BD9(B $B>.NS(B $BLwOB!&%9%_%9(B $B%j%A%c!<%I(B) | |||||
C29 | $B%^%$%/%m<><0KB;e%W%m%;%9$K$h$k%]%j%"%_%C%/;@A!0]$ND4@=$H5!G=@-I>2A(B | Microfluidic device Nanofiber Tensile test | 5-f | 107 | |
C30 | $B%^%$%/%m<><0KB;e$K$h$k%9%F%l%*%3%s%W%l%C%/%9%]%jF};@%U%!%$%P!<$ND4@=(B | Microchannel wet-spinning process Stereocomplex PLA | 5-f | 113 | |
C31 | CNF$B?eJ,;61U$r86NA$H$7$?%^%$%/%m<><0KB;e%W%m%;%9$K$h$k%;%k%m!<%9A!0]$ND4@=(B | Microfluidic device Jet flow CNF dispersion | 5-f | 115 | |
C32 | $BB?7k>=(BSiC-CVD$B%W%m%;%9@_7W$N$?$a$NAm3gH?1~%b%G%k9=C[(B~(1)$B05NO0MB8@-(B~ | Chemical Vapor Deposition Silicon Carbide macrocavity method | 5-h | 132 | |
C33 | $B86;RAXBO@QK!$K$h$k(BCo$BGvKl7A@.$N4pAC8!F$(B | ALD Cobalt thin film initial growth | 5-h | 255 | |
C34 | $BG.J,2rC:AG$N?e>x5$%,%92=H?1~B.EY$NDj<02=(B | CVD Carbon Steam | 5-h | 256 |