$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cH?1~9)3X$N?7$7$$E83+!d(B | |||||
(9:20$B!A(B10:40)$B!!(B($B:BD9(B $B4_ED!!>;9@(B) | |||||
Q102 | $B0eLtIJ%?%s%Q%/ | Micron-size device surface material aqueous polymer two-phase systems | S-12 | 943 | |
Q103 | $B%R%H(BDNase_I$B@8;:MQ9ZJl$rMQ$$$?%^%$%/%m6u4VFb@8J*H?1~$N2r@O(B | $B%^%$%/%m@8J*H?1~4o(B $B2sJ,G]M\(B $BO"B3G]M\(B | S-12 | 244 | |
Q104 | $B1UAj%^%$%/%m%j%"%/%?!<$G$NFs2A(B-$B3H;6$N1F6A(B | microreactor rapid reaction diffusion | S-12 | 145 | |
Q105 | $B1UAj%^%$%/%m%j%"%/%?!<$G$NC`2A(B-$B3H;6$NA*Br@-$X$N1F6A(B | microreactor consecutive reaction transport phenomena | S-12 | 156 | |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $BJ!86!!D9 | |||||
Q106 | $B9b299b05%^%$%/%m%_%-%5!<$N3+H/(B | micromixer high pressure and temperature supercritical fluid | S-12 | 85 | |
Q107 | $BHsEy297O$K$*$1$kN.BN%;%0%a%s%H$K4p$E$$$?:.9g!&H?1~A`:n$N@_7W(B | microreactor fluid segment nonisothermal operation | S-12 | 38 | |
Q108 | $BN.BN%;%0%a%s%H>WFM$K4p$E$$$?%^%$%/%m%_%-%5!<$K$h$k%S%9%U%'%N!<%k(BF$B$N9g@.(B | micromixer bisphenol F selectivity | S-12 | 37 | |
Q109 | $B%^%$%/%m=E9gH?1~%7%9%F%`$rMQ$$$?9bJ,;RHyN3;R$NN37B@)8f$N;n$_(B | microreactor soap free polymerization suspension polymerization | S-12 | 86 | |
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $BKR(B $BBYJe(B) | |||||
Q113 | $B%^%$%/%m%A%c%M%k$rMxMQ$7$?HyNL1UBN$N>xN1(B | distillation microchannel microreactor | S-12 | 984 | |
Q114 | $B5$8G?(G^H?1~7O$K$*$1$k%^%$%/%m%A%c%M%kJILLC4;}?(G^$K4X$9$k9M;!(B | micro channel catalyst gas solid reaction | S-12 | 755 | |
Q115 | $B%>%k%2%kK!$rMxMQ$7$?%^%$%/%m%A%c%M%k?(G^$N:n@=(B | catalyst microchannel sol gel | S-12 | 259 | |
Q116 | $B%^%$%/%m%j%"%/%?!<$N$?$a$NGr6b(B-$B%"%k%_%J?(G^$X$N%"%k%+%j6bB0E:2C$N1F6A(B | microreactor catalyst alkali | S-12 | 60 | |
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $B4X!! | |||||
Q117 | $B%^%$%/%m%A%e!<%V7?(BPd-Zn$B7O?(G^$K$h$k%a%?%N!<%k$N?e>x5$2~ | Microreactor Methanol steam-reforming Pd-Zn catalyst | S-12 | 355 | |
Q118 | $B%8%a%A%k%(!<%F%k2~u$K$h$k3h@-$X$N1F6A(B | dimethylether steam reforming catalyst | S-12 | 383 | |
Q119 | $BG3NAEECSMQ%8%a%A%k%(!<%F%k?e>x5$2~ | DME CFD reforming | S-12 | 200 | |
(15:20$B!A(B16:40)$B!!(B($B:BD9(B $BC]Cf!!AT(B) | |||||
Q120 | $B%"%k%^%$%H?(G^$rMQ$$$?7HBS5!4o8~$1G3NAEECSMQ%^%$%/%m2~ | Almite Catalyst Micro Reactor Steam Reforming | S-12 | 640 | |
Q121 | $B?(G^0lBN2=%b%8%e!<%k$N3+H/(B | Hydrogen Membrane Reformer | S-12 | 426 | |
Q122 | Ru/ZrO2$B?(G^>e$G$N%a%?%s$N9b05?e>x5$2~ | Methane steam reforming High pressure Initial reaction rate | S-12 | 170 | |
Q123 | $B2~2A(B | Palladium Alloy Membrane Impurity Gas Surface Reaction | S-12 | 430 | |
(16:40$B!A(B17:40)$B!!(B($B:BD9(B $BApJI!!9n8J(B) | |||||
Q124 | CO$B$NA*Br;@2=$N$?$a$N%^%$%/%m%A%e!<%V>u?(G^$ND4@=(B | Microreactor Preferential CO oxidation Co/Al catalyst | S-12 | 357 | |
Q125 | $B%8%a%A%k%(!<%F%k6&B82<$K$*$1$k(BCO$BA*Br;@2=H?1~FC@-(B | dimethylether preferential oxidation catalyst | S-12 | 512 | |
Q126 | $B@PL}7OC:2=?eAG$NJ,2rK!$K$h$k(BCOx$B%U%j! | nickel COx-free hydrogen hydrocarbon decomposition | S-12 | 571 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cH?1~9)3X$N?7$7$$E83+!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BB?8P!!516=(B) | |||||
Q201 | C12A7$B8GBNFb$N3h@-;@AG$rMQ$$$?(BVOC$B;@2=H?1~$NDc292=(B | active oxygen species C12A7 VOC | S-12 | 688 | |
Q202 | C12A7$B$+$i$N(BO-$B@8@.$NDc292=(B | C12A7 oxygen anion radical | S-12 | 740 | |
Q203 | O-$B$N1UAjH?1~$N5sF0$K$D$$$F(B | oxygen anion radical ion reaction pH | S-12 | 762 | |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B@>2,!!>-51(B) | |||||
Q204 | HCFC-22$B$NJ,2rB.EY$K$*$1$k(BNaOH$B$N1F6A(B | HCFC-22 vapor-liquid equilibrium reaction rate controlling | S-12 | 14 | |
Q205 | $B9b;@AGG;EY2<$G$NL5?(G^C&>K$K$*$1$k(BNOx$BH?1~5!9=$N8!F$(B | non-catalytic reduction NOx mechanism | S-12 | 865 | |
Q206 | $B%j%s;@%^%0%M%7%&%`4XO"2=9gJ*$K$h$k%"%s%b%K%"$NO"B32s<}$N;n$_(B | removal and recovery aqueous ammonium magnesium phosphates | S-12 | 56 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B30NX!!7r0lO:(B) | |||||
Q207 | $B%j%s;@%^%0%M%7%&%`%"%s%b%K%&%`$K$h$k%P%$%*%^%9GQ4~J*$+$i$N%"%s%b%K%"2s<}(B | Biomass ammonia MAP | S-12 | 260 | |
Q208 | Ni-Y$B7?%<%*%i%$%H$K$h$k?eAjCf4uGv%A%*%U%'%N!<%k9b8zN(=|5n(B | bio-polyester thiophenol Ni-Y type zeolite | S-12 | 263 | |
Q209 | Reaction Kinetics of the synthesis of a novel biodegradable plastic using a water-soluble protein under the sub-critical water condition | Sub-critical water Reaction engineering biodegradable plastic | S-12 | 516 | |
(14:40$B!A(B15:20)$B!!(B($B;J2q(B $B4_ED!!>;9@(B) | |||||
Q218 | [$BE8K>9V1i(B]$B%"%b%k%U%!%99g6b$r86NA$H$9$k?(G^D4@=5;=Q$NE8K>(B | S-12 | 768 | ||
(15:20$B!A(B16:00)$B!!(B($B;J2q(B $B8^==Mr!!E/(B) | |||||
Q220 | [$BE8K>9V1i(B]$B?e>x5$2~ | Pre-reforming 10-Hole shape ISOP catalyst | S-12 | 750 | |
(16:00$B!A(B16:40)$B!!(B($B;J2q(B $BA}ED!!N4IW(B) | |||||
Q222 | [$BE8K>9V1i(B]10$BG/8e$N9)6H?(G^(B | Changing Market New catalysts Catalyst industry | S-12 | 753 | |
(16:40$B!A(B17:20)$B!!(B($B;J2q(B $BED@n!!CRI'(B) | |||||
Q224 | [$BE8K>9V1i(B]$B%(%s%8%K%"%j%s%0$+$i8+$??(G^$HH?1~4o$N@_7W(B | Structure of Catalytic Reactor Simulation Design of Catalytic Reactor | S-12 | 760 |