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9:20$B!A(B 9:40 | Q102 | $B0eLtIJ%?%s%Q%/ ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$B7,86(B $BOB9((B$B!&(B($B@5(B)$B@u8+(B $BOB9-(B$B!&(B($B@5(B)$BB@ED8}(B $BOB5W(B | Micron-size device surface material aqueous polymer two-phase systems
| S-12 | 943 |
9:40$B!A(B 10:00 | Q103 | $B%R%H(BDNase_I$B@8;:MQ9ZJl$rMQ$$$?%^%$%/%m6u4VFb@8J*H?1~$N2r@O(B ($BEl9)Bg1!(B) $B>.NS(B $BM50l(B$B!&(B$B!{(B($B@5(B)$B@u8+(B $BOB9-(B$B!&(B($B@5(B)$BB@ED8}(B $BOB5W(B | $B%^%$%/%m@8J*H?1~4o(B $B2sJ,G]M\(B $BO"B3G]M\(B
| S-12 | 244 |
10:00$B!A(B 10:20 | Q104 | $B1UAj%^%$%/%m%j%"%/%?!<$G$NFs2A(B-$B3H;6$N1F6A(B ($B9)3X1!Bg1!9)(B) $B!{:4F#(B $B=a(B$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$BBgM'(B $B=g0lO:(B$B!&(B($B9b05%,%9J]0B6(2q(B) ($B@5(B)$BBgEg(B $B\F$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$BD9K\(B $B1Q=S(B | microreactor rapid reaction diffusion
| S-12 | 145 |
10:20$B!A(B 10:40 | Q105 | $B1UAj%^%$%/%m%j%"%/%?!<$G$NC`2A(B-$B3H;6$NA*Br@-$X$N1F6A(B ($B9)3X1!Bg1!9)(B) $B!{:4F#(B $B=a(B$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$BBgM'(B $B=g0lO:(B$B!&(B($B9b05%,%9J]0B6(2q(B) ($B@5(B)$BBgEg(B $B\F$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$BD9K\(B $B1Q=S(B | microreactor consecutive reaction transport phenomena
| S-12 | 156 |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $BJ!86!!D9 |
10:40$B!A(B 11:00 | Q106 | $B9b299b05%^%$%/%m%_%-%5!<$N3+H/(B ($B5~Bg9)(B) $B!{(B($B@5(B)$BA0(B $B0lW"(B$B!&(B($B@5(B)$BKR(B $BBYJe(B$B!&(B($B3X(B)$B:4F#(B $B85(B$B!&(B($B;:Am8&ElKL(B) ($B@5(B)$BNkLZ(B $BL@(B$B!&(B($B@5(B)$BGlED(B $B9,Li(B$B!&(B($B@5(B)$B?70f(B $BK.IW(B$B!&(B($BElKLBg9)(B) ($B@5(B)$BCv8T(B $B9((B | micromixer high pressure and temperature supercritical fluid
| S-12 | 85 |
11:00$B!A(B 11:20 | Q107 | $BHsEy297O$K$*$1$kN.BN%;%0%a%s%H$K4p$E$$$?:.9g!&H?1~A`:n$N@_7W(B ($B5~Bg9)(B) $B!{(B($B3X(B)$B@DLZ(B $B@kL@(B$B!&(B($B@5(B)$BA0(B $B0lW"(B | microreactor fluid segment nonisothermal operation
| S-12 | 38 |
11:20$B!A(B 11:40 | Q108 | $BN.BN%;%0%a%s%H>WFM$K4p$E$$$?%^%$%/%m%_%-%5!<$K$h$k%S%9%U%'%N!<%k(BF$B$N9g@.(B ($B?7F|oD2=3X(B) $BBgEl(B $B>:(B$B!&(B($B5~Bg9)(B) $B!{(B($B3X(B)$B@DLZ(B $B@kL@(B$B!&(B$B5HED(B $B=a0l(B$B!&(B($B@5(B)$BA0(B $B0lW"(B | micromixer bisphenol F selectivity
| S-12 | 37 |
11:40$B!A(B 12:00 | Q109 | $B%^%$%/%m=E9gH?1~%7%9%F%`$rMQ$$$?9bJ,;RHyN3;R$NN37B@)8f$N;n$_(B ($B5~Bg9)(B) ($B@5(B)$BKR(B $BBYJe(B$B!&(B$B!{(B($B3X(B)$BNS(B $BC#Li(B$B!&(B($B3X(B)$BCf@>(B $BJ8?M(B$B!&(B($B@5(B)$BBg5WJ](B $B>0?M(B$B!&(B($B@5(B)$BA0(B $B0lW"(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) |
13:00$B!A(B 13:20 | Q113 | $B%^%$%/%m%A%c%M%k$rMxMQ$7$?HyNL1UBN$N>xN1(B ($B:eI\Bg9)(B) $B!{(B($B3X(B)$B4dDZ(B $BM$Ka(B$B!&(B($BElBg9)(B) ($B3X(B)$B;3ED(B $B??@!(B$B!&(B($B:eI\Bg9)(B) ($B@5(B)$B0BED(B $B>;90(B$B!&(B($B@5(B)$B4X(B $B | distillation microchannel microreactor
| S-12 | 984 |
13:20$B!A(B 13:40 | Q114 | $B5$8G?(G^H?1~7O$K$*$1$k%^%$%/%m%A%c%M%kJILLC4;}?(G^$K4X$9$k9M;!(B ($BEl$B!&(B($BJ!2,=wBg(B) ($B@5(B)$BApJI(B $B9n8J(B | micro channel catalyst gas solid reaction
| S-12 | 755 |
13:40$B!A(B 14:00 | Q115 | $B%>%k%2%kK!$rMxMQ$7$?%^%$%/%m%A%c%M%k?(G^$N:n@=(B ($BJ!=wBg?M4V4D6-(B) $B!{(B($B3X(B)$B5\ED(B $B:L;R(B$B!&(B($B2,;3;:6H?66=:bCD(B) ($B@5(B)$B-;L(B$B!&(B($BJ!=wBg?M4V4D6-(B) ($B@5(B)$BApJI(B $B9n8J(B | catalyst microchannel sol gel
| S-12 | 259 |
14:00$B!A(B 14:20 | Q116 | $B%^%$%/%m%j%"%/%?!<$N$?$a$NGr6b(B-$B%"%k%_%J?(G^$X$N%"%k%+%j6bB0E:2C$N1F6A(B ($BL>Bg9)(B) $B!{(B($B3X(B)$BEOn5(B $BM55*(B$B!&(B($B@5(B)$BED@n(B $BCRI'(B$B!&(B($B@5(B)$B;3ED(B $BGn;K(B | microreactor catalyst alkali
| S-12 | 60 |
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $B4X!! |
14:20$B!A(B 14:40 | Q117 | $B%^%$%/%m%A%e!<%V7?(BPd-Zn$B7O?(G^$K$h$k%a%?%N!<%k$N?e>x5$2~ ($BH,8M9)Bg9)(B) $B!{(B($B3X(B)$B3yED(B $B2BG7(B$B!&(B($B@5(B)$BJ!86(B $BD9$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$B8^==Mr(B $BE/(B | Microreactor Methanol steam-reforming Pd-Zn catalyst
| S-12 | 355 |
14:40$B!A(B 15:00 | Q118 | $B%8%a%A%k%(!<%F%k2~u$K$h$k3h@-$X$N1F6A(B ($BEl$B!&(B($B@5(B)$B;3ED(B $BOBLp(B$B!&(B$BKRLn(B $B?70l(B$B!&(B($B@5(B)$B5HLn(B $B@5?M(B$B!&(B$BJ!Eg(B $B8x?F(B | dimethylether steam reforming catalyst
| S-12 | 383 |
15:00$B!A(B 15:20 | Q119 | $BG3NAEECSMQ%8%a%A%k%(!<%F%k?e>x5$2~ ($BF|4x(B) $B!{9b66(B $B8x5*(B$B!&(B$B;32P(B $B5.5A(B | DME CFD reforming
| S-12 | 200 |
(15:20$B!A(B16:40)$B!!(B($B:BD9(B $BC]Cf!!AT(B) |
15:20$B!A(B 15:40 | Q120 | $B%"%k%^%$%H?(G^$rMQ$$$?7HBS5!4o8~$1G3NAEECSMQ%^%$%/%m2~ ($BElG@9)Bg9)(B) $B!{(B($B3X(B)$BEDBe(B $B$5$H$_(B$B!&(B($B?7F|K\@PL}(B) ($B@5(B)$B;T@n(B $B4vM:(B$B!&(B($BElG@9)Bg9)(B) ($B@5(B)$B:y0f(B $B@?(B$B!&(B($B@5(B)$BKLEg(B $BDwFs(B$B!&(B($B@5(B)$B55;3(B $B=(M:(B | Almite Catalyst Micro Reactor Steam Reforming
| S-12 | 640 |
15:40$B!A(B 16:00 | Q121 | $B?(G^0lBN2=%b%8%e!<%k$N3+H/(B ($BEl5~%,%9(B) $B!{>oLZ(B $BC#Li(B$B!&(B($B@5(B)$BGr:j(B $B5AB'(B$B!&(B$BB@ED(B $BMN=#(B$B!&(B$B0BED(B $BM&(B$B!&(B($BF|K\FC$B!&(B$B;V3@(B $B=(OB(B$B!&(B$BEDCf(B $BM5G7(B$B!&(B$B;0Lp(B $B9LJ?(B | Hydrogen Membrane Reformer
| S-12 | 426 |
16:00$B!A(B 16:20 | Q122 | Ru/ZrO2$B?(G^>e$G$N%a%?%s$N9b05?e>x5$2~ ($B9)3X1!Bg9)(B) $B@jIt(B $BM4(B$B!&(B$B!{(B($B@5(B)$B8^==Mr(B $BE/(B | Methane steam reforming High pressure Initial reaction rate
| S-12 | 170 |
16:20$B!A(B 16:40 | Q123 | $B2~2A(B ($BElKLBgB?858&(B) $B!{(B($B3X(B)$B1':,K\(B $BFF(B$B!&(B$B3+JF(B $BFF;V(B$B!&(B$B:4F#(B $B0l1J(B$B!&(B$BBgC](B $BN47{(B$B!&(B$BH,Be(B $B7=;J(B$B!&(B$B@nED(B $BC#Li(B$B!&(B$B?e:j(B $B=c0lO:(B$B!&(B($BEl5~%,%9(B) $B>oLZ(B $BC#Li(B$B!&(B$BGr:j(B $B5AB'(B$B!&(B$B0BED(B $BM&(B | Palladium Alloy Membrane Impurity Gas Surface Reaction
| S-12 | 430 |
(16:40$B!A(B17:40)$B!!(B($B:BD9(B $BApJI!!9n8J(B) |
16:40$B!A(B 17:00 | Q124 | CO$B$NA*Br;@2=$N$?$a$N%^%$%/%m%A%e!<%V>u?(G^$ND4@=(B ($BH,8M9)Bg9)(B) $B!{(B($B3X(B)$BEDC<(B $B3X(B$B!&(B($B@5(B)$BJ!86(B $BD9$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$B8^==Mr(B $BE/(B | Microreactor Preferential CO oxidation Co/Al catalyst
| S-12 | 357 |
17:00$B!A(B 17:20 | Q125 | $B%8%a%A%k%(!<%F%k6&B82<$K$*$1$k(BCO$BA*Br;@2=H?1~FC@-(B ($BEl$B!&(B$B>>1J(B $B7rB@O:(B$B!&(B($B@5(B)$BLx@8(B $B4pLP(B$B!&(B($B@5(B)$B;3ED(B $BOBLp(B$B!&(B$BJ!Eg(B $B8x?F(B | dimethylether preferential oxidation catalyst
| S-12 | 512 |
17:20$B!A(B 17:40 | Q126 | $B@PL}7OC:2=?eAG$NJ,2rK!$K$h$k(BCOx$B%U%j! ($B6eBg1!9)(B) $B!{(B($B3X(B)$B2OEg(B $B7r<#(B$B!&(B($B@5(B)$B>>:,(B $B1Q$B!&(B($B@5(B)$BC]Cf(B $BAT(B$B!&(B($B@5(B)$B4_ED(B $B>;9@(B | nickel COx-free hydrogen hydrocarbon decomposition
| S-12 | 571 |
Q$B2q>l(B $BBh(B2$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BB?8P!!516=(B) |
9:00$B!A(B 9:20 | Q201 | C12A7$B8GBNFb$N3h@-;@AG$rMQ$$$?(BVOC$B;@2=H?1~$NDc292=(B ($B;:Am8&(B) $B!{(B($B@5(B)$B@>2,(B $B>-51(B$B!&(B($BElKL3X1!Bg(B) $B2f:J(B $B@.=)(B$B!&(B($B;:Am8&(B) $B3k@>(B $B??6W(B | active oxygen species C12A7 VOC
| S-12 | 688 |
9:20$B!A(B 9:40 | Q202 | C12A7$B$+$i$N(BO-$B@8@.$NDc292=(B ($B9)3X1!Bg9)(B) $B!{0$H~(B $BM!(B$B!&(B($B@5(B)$BDjJ}(B $B@55#(B | C12A7 oxygen anion radical
| S-12 | 740 |
9:40$B!A(B 10:00 | Q203 | O-$B$N1UAjH?1~$N5sF0$K$D$$$F(B ($B9)3X1!Bg9)(B) $B!{Bg?9(B $B3Y(B$B!&(B($B@5(B)$BDjJ}(B $B@55#(B | oxygen anion radical ion reaction pH
| S-12 | 762 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B@>2,!!>-51(B) |
10:00$B!A(B 10:20 | Q204 | HCFC-22$B$NJ,2rB.EY$K$*$1$k(BNaOH$B$N1F6A(B ($BK!@/Bg9)(B) $B!{(B($B3X(B)$B>.3^86(B $B42$B!&(B($B@5(B)$B@>3$(B $B1QM:(B | HCFC-22 vapor-liquid equilibrium reaction rate controlling
| S-12 | 14 |
10:20$B!A(B 10:40 | Q205 | $B9b;@AGG;EY2<$G$NL5?(G^C&>K$K$*$1$k(BNOx$BH?1~5!9=$N8!F$(B ($BElBg1!9)(B) $B!{(B($B@5(B)$B;3K\(B $B8wIW(B$B!&(B($B;00fB$A%(B) $B0qLZ(B $B>40l(B$B!&(B($BElBg1!9)(B) ($B@5(B)$B1[(B $B8wCK(B | non-catalytic reduction NOx mechanism
| S-12 | 865 |
10:40$B!A(B 11:00 | Q206 | $B%j%s;@%^%0%M%7%&%`4XO"2=9gJ*$K$h$k%"%s%b%K%"$NO"B32s<}$N;n$_(B ($BFAEgBg9)(B) $B!{(B($B@5(B)$B?y;3(B $BLP(B$B!&(B$B2#;3(B $B2mI'(B$B!&(B($B@5(B)$B30NX(B $B7r0lO:(B | removal and recovery aqueous ammonium magnesium phosphates
| S-12 | 56 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B30NX!!7r0lO:(B) |
11:00$B!A(B 11:20 | Q207 | $B%j%s;@%^%0%M%7%&%`%"%s%b%K%&%`$K$h$k%P%$%*%^%9GQ4~J*$+$i$N%"%s%b%K%"2s<}(B ($BKLBg1!9)(B) $B!{(B($B3X(B)$BO<(B $B7CN$(B$B!&(B($B@5(B)$BB?8P(B $B516=(B$B!&(B($B@5(B)$BA}ED(B $BN4IW(B | Biomass ammonia MAP
| S-12 | 260 |
11:20$B!A(B 11:40 | Q208 | Ni-Y$B7?%<%*%i%$%H$K$h$k?eAjCf4uGv%A%*%U%'%N!<%k9b8zN(=|5n(B ($BKLBg1!9)(B) $B!{(B($B@5(B)$BB?8P(B $B516=(B$B!&(B($B3X(B)$Bc7F#(B $BAoIR(B$B!&(B$BEDEg(B $B7r$B!&(B$BED8}(B $B@:0l(B$B!&(B$B:4F#(B $BIRJ8(B$B!&(B$B:4F#(B $B9/<#(B$B!&(B($B@5(B)$BA}ED(B $BN4IW(B | bio-polyester thiophenol Ni-Y type zeolite
| S-12 | 263 |
11:40$B!A(B 12:00 | Q209 | Reaction Kinetics of the synthesis of a novel biodegradable plastic using a water-soluble protein under the sub-critical water condition (Osaka Prefectuer U.) $B!{(B($B@5(B)Abdelmoez Wael$B!&(B($B@5(B)Yoshida Hiroyuki | Sub-critical water Reaction engineering biodegradable plastic
| S-12 | 516 |
|
(14:40$B!A(B15:20)$B!!(B($B;J2q(B $B4_ED!!>;9@(B) |
14:40$B!A(B 15:20 | Q218 | [$BE8K>9V1i(B]$B%"%b%k%U%!%99g6b$r86NA$H$9$k?(G^D4@=5;=Q$NE8K>(B ($B$B!&(B($B@5(B)$B9CHe(B $B7IH~(B |
| S-12 | 768 |
(15:20$B!A(B16:00)$B!!(B($B;J2q(B $B8^==Mr!!E/(B) |
15:20$B!A(B 16:00 | Q220 | [$BE8K>9V1i(B]$B?e>x5$2~ ($B%:!<%I%1%_!(G^(B) $B!{>>5W(B $BIRM:(B | Pre-reforming 10-Hole shape ISOP catalyst
| S-12 | 750 |
(16:00$B!A(B16:40)$B!!(B($B;J2q(B $BA}ED!!N4IW(B) |
16:00$B!A(B 16:40 | Q222 | [$BE8K>9V1i(B]10$BG/8e$N9)6H?(G^(B ($B%(%L!&%$!<%1%`%-%c%C%H(B) $B!{<<0f(B $B|b>k(B | Changing Market New catalysts Catalyst industry
| S-12 | 753 |
(16:40$B!A(B17:20)$B!!(B($B;J2q(B $BED@n!!CRI'(B) |
16:40$B!A(B 17:20 | Q224 | [$BE8K>9V1i(B]$B%(%s%8%K%"%j%s%0$+$i8+$??(G^$HH?1~4o$N@_7W(B ($BF|4x(B) $B!{CvKs(B $B@?(B | Structure of Catalytic Reactor Simulation Design of Catalytic Reactor
| S-12 | 760 |
R$B2q>l(B $BBh(B1$BF|(B |
(9:20$B!A(B10:40)$B!!(B($B:BD9(B $B9CHe!!7IH~(B) |
9:20$B!A(B 9:40 | R102 | $B%"%k%_%JC4BN>e$N6bB0(BCo$B$H(BRu$B$NAj8_G[CV@)8f(B ($B6eBg1!9)(B) $BOBCR(B $B@k9T(B$B!&(B$B1|20(B $B5.Bg(B$B!&(B($B@5(B)$B>>:,(B $B1Q$B!&(B$B!{(B($B@5(B)$BC]Cf(B $BAT(B$B!&(B($B@5(B)$B4_ED(B $B>;9@(B | alumina-supprted Co Ruthenium addition CO hydrogenation
| S-12 | 560 |
9:40$B!A(B 10:00 | R103 | $B%a%?%sItJ,;@2=$KBP$9$k%7%j%+HoJ$%K%C%1%k?(G^$NBQ5W@-$N8!F$(B ($B6eBg1!9)(B) $B!{(B($B3X(B)$BG_NS(B $B9-(B$B!&(B($B@5(B)$B>>:,(B $B1Q$B!&(B($B@5(B)$BC]Cf(B $BAT(B$B!&(B($B@5(B)$B4_ED(B $B>;9@(B | silica-coated Ni silica-supported Ni partial oxidation of methane
| S-12 | 461 |
10:00$B!A(B 10:20 | R104 | $B?e(B/$BM-5!MOG^(B/$B3&LL3h@-:^MO1U$rH?1~>l$H$7$?%<%*%i%$%H%J%N%/%j%9%?%k9g@.K!(B ($BKLBg1!9)(B) $B!{(B($B3X(B)$B4d3-(B $BOB9,(B$B!&(B($B3X(B)$B@DLZ(B $BBgCO(B$B!&(B($B@5(B)$BB?8P(B $B516=(B$B!&(B($B@5(B)$BA}ED(B $BN4IW(B | zeolite nanocrystal surfactant
| S-12 | 875 |
10:20$B!A(B 10:40 | R105 | $B<+F0 ($BL>Bg(B) $B!{(B($B3X(B)$BHx4X(B $B90=$(B$B!&(B($B@5(B)$B;3ED(B $BGn;K(B$B!&(B($B@5(B)$BED@n(B $BCRI'(B$B!&(B($BK-EDCf8&(B) ($B@5(B)$B9b66(B $BD> | diffusion coefficient automotive catalysts gas
| S-12 | 882 |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $B;3ED!!Gn;K(B) |
10:40$B!A(B 11:00 | R106 | $BC4;}5.6bB0?(G^>e$G$N(BNO-CO$BH?1~$K$*$1$k<~4|E*(BO2$BE:2C8z2L(B ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$B9b66(B $B@?(B$B!&(B(KMITL) Yuangsawad R$B!&(B($B@5(B)Na-Ranonga D$B!&(B($BEl9)Bg1!M}9)(B) ($B@5(B)$BAjED(B $BN4;J(B | Periodic Operation NO-CO-O$2$ Reaction Noble Metal
| S-12 | 776 |
11:00$B!A(B 11:20 | R107 | $B;@2=E4$N4T85!&:F;@2=$NB.EYO@E*8!F$$K4p$E$/5<;w0\F0AX7?H?1~4o@_7W(B ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$B:#@>(B $B9(FA(B$B!&(B($B@5(B)$BAjED(B $BN4;J(B | hydrogn storage iron oxide simulated moving bed reactor
| S-12 | 789 |
11:20$B!A(B 11:40 | R108 | Bi-P-O$B?(G^;@2=EY$X$NN.NL$N1F6A$H<~4|E*N.NLJQF0A`:n$X$N1~MQ(B ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BKY9>(B $B9';K(B$B!&(B($B@5(B)$BAjED(B $BN4;J(B | Bi-P-O catalyst gas velocity forced flow rate cycling
| S-12 | 817 |
11:40$B!A(B 12:00 | R109 | $BBN@Q8:>/$r4^$`H?1~$rN.F0?(G^AX$G9T$&>l9g$NH?1~%,%9B?CJ6!5k$N8z2L(B ($B$B!&(B$BDL;3(B $B7C0l(B$B!&(B$BKYG7Fb(B $B=_J?(B$B!&(B($B@5(B)$B9b66(B $BIp=E(B$B!&(B($B@P@nEg%W%i%s%H%(%s%8%K%"%j%s%0(B) $BCfEg(B $B=<9,(B | reactor fluidized bed defluidization
| S-12 | 83 |
|
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B0BED!!7<;J(B) |
13:00$B!A(B 13:20 | R113 | $B%^%$%/%mGH>H ($BF|N)%W%i%s%H%F%/%N%m%8!<(B) $B!{(B($B@5(B)$BKv>>(B $B9'>O(B$B!&(B($B0&I2Bg(B) $B5H2,(B $B?5;T(B$B!&(B$BCfLp(B $B1Q0t(B$B!&(B$B>.Eg(B $B=(;R(B | microwave aromatic compound alkylation
| S-12 | 57 |
13:20$B!A(B 13:40 | R114 | $BD62;GH>HmCf$K;DN1$9$kM-5!1vAG7O=|Ap:^$NCj=P$*$h$SJ,2r(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$BF#ED(B $BN4J8(B$B!&(B($BL>Bg9)(B) ($B@5(B)$B>>ED(B $B?N$B!&(B($BL>Bg%(%3%H%T%"(B) ($B@5(B)$B>.Eg(B $B5A90(B$B!&(B($BK\B?EE;R(B) $BD+AR(B $B5A9,(B | ultrasound extraction organo-chlorine herbicide
| S-12 | 287 |
13:40$B!A(B 14:00 | R115 | $B%A%e!<%V7?KlH?1~4o$KE,9g$7$?%^%$%/%mGH2CG.AuCV$N3+H/(B ($B;:Am8&(B) $B!{(B($B@5(B)$B@>2,(B $B>-51(B$B!&(B$B3k@>(B $B??6W(B$B!&(BTanaka Pacheco Alfredo$B!&(B$B?e>e(B $BIZ;NIW(B | microwave membrane reactor palladium
| S-12 | 699 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B>.Eg(B $B5A90(B) |
14:00$B!A(B 14:20 | R116 | $BBg7?$ND62;GHH?1~4o$N3+H/(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$B2CF#(B $BBg51(B$B!&(B($BK\B?EE;R(B) ($B@5(B)$BD+AR(B $B5A9,(B$B!&(B($BL>Bg1!9)(B) ($B@5(B)$B0BED(B $B7<;J(B$B!&(B($B@5(B)$BKYE:(B $B9@=S(B$B!&(B($B@5(B)$B9aED(B $BG&(B | ultrasonic reactor superposition large-scale
| S-12 | 369 |
14:20$B!A(B 14:40 | R117 | $B%(%?%N!<%k$ND62;GHL82=J,N%$K$*$1$k>xH/$N1F6A(B ($BL>Bg1!(B) $B!{(B($B3X(B)$BEZ4t(B $BH~Nk(B$B!&(B($B@5(B)$BFs0f(B $B?8(B$B!&(B($B@5(B)$B@n@t(B $BJ8CK(B$B!&(B($BD62;GH>zB$=j(B) ($B@5(B)$B>>1:(B $B0lM:(B$B!&(B($B@5(B)$B? | ultrasonic atomization evaporation ethanol
| S-12 | 428 |
14:40$B!A(B 15:00 | R118 | $BD62;GH$rMQ$$$?%(%^%k%7%g%s$+$i$NL}AjJ,N%B%?J(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$B5FK\(B $B=S2p(B$B!&(B($B@5(B)$BFs0f(B $B?8(B$B!&(B($B@5(B)$BFA;3(B $B1QL@(B$B!&(B($B@5(B)$B@n@t(B $BJ8CK(B | ultrasonic separation emulsion coalescence
| S-12 | 617 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BGr@P!!J8=((B) |
15:00$B!A(B 15:20 | R119 | $BFs;@2=%A%?%s!&D62;GHK!$K$h$k(BOH$B%i%8%+%k$N@8@.$HMOB8%"%k%4%s$NB%?J8z2L(B ($B6bBtBg1!<+A32J(B) $B!{(B($B3X(B)$BF#J?(B $BFX;J(B$B!&(B($B3X(B)$B:j;3(B $BOB5}(B$B!&(B($B@5(B)$B2.Ln(B $B@i=)(B$B!&(B($B6bBtBg<+A37WB,1~MQ8&5f%;%s%?!<(B) ($B@5(B)$B@6?e(B $B@kL@(B | TiO2 cavitation ultrasound
| S-12 | 716 |
15:20$B!A(B 15:40 | R120 | $B?e$N2D;k8wJ,2r%b%G%k$K$*$1$k8w?(G^@QAXKl$N9=C[(B ($B;37ABg9)(B) $B!{(B($B3X(B)$BCfLn(B $B>08c(B$B!&(B$B>!;3(B $BE/M:(B$B!&(B($B@5(B)$B9bH*(B $BJ]G7(B$B!&(B($B@5(B)$B>>ED(B $BNI90(B | Photolysis of Water Titania Platinum
| S-12 | 142 |
15:40$B!A(B 16:00 | R121 | $B9b5!G=8w?(G^6t$K$h$k%[%k%`%"%k%G%R%I$N=|5n(B ($BJ!2,Bg9)(B) $B!{(B($B3X(B)$BBgDM(B $BNIJ?(B$B!&(B($B@5(B)$BBg^<(B $B1Q;R(B$B!&(B($B@5(B)$BCfLn(B $B>!G7(B | TiO2 photocatalyst zeolite lime plaster
| S-12 | 367 |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $BBg^ |
16:00$B!A(B 16:20 | R122 | $B>.7?2=$7$?JBNs4I7?8w?(G^H?1~4o$N@-G=I>2A(B ($B6eBg%P%$%*%"!<%/(B) $B!{(B($B@5(B)$BGr@P(B $BJ8=((B$B!&(B($B6e9)Bg>p9)(B) $B>e2>20(B $BD>Li(B$B!&(B($B%"%$%/%)!<%/(B) $BN)@P(B $B7{<#(B$B!&(B($B%"%k%9%j%5!<%A(B) $B;3K\(B $B=(G7(B | Compacted photocatalytic reactor Volatile organic compounds PET film
| S-12 | 339 |
16:20$B!A(B 16:40 | R123 | $BJBNs4I7?8w?(G^H?1~4o$K$h$kL)JD6u4VFb$N6u5$CfHyNL%H%k%(%sJ,2r$HLdBjE@(B ($B6eBg%P%$%*%"!<%/(B) ($B@5(B)$BGr@P(B $BJ8=((B$B!&(B$B!{@P>>(B $B9'>O(B$B!&(B($B6e9)Bg>p9)(B) $B>e2>20(B $BD>Li(B | Photocatalytic reacto Toluene Adsorption
| S-12 | 341 |
16:40$B!A(B 17:00 | R124 | $BMO ($B6eBg%P%$%*%"!<%/(B) ($B@5(B)$BGr@P(B $BJ8=((B$B!&(B$B!{(B($B3X(B)$B0KF#(B $B7r(B$B!&(B($B%U%8%3!<(B) $B1J5H(B $B1Q><(B$B!&(B$BHu8}(B $BM'I'(B$B!&(B($B%"%$%/%)!<%/(B) $BN)@P(B $B7{<#(B | Photocatalyst Thermal spraying Water treatment
| S-12 | 344 |
(17:00$B!A(B17:40)$B!!(B($B:BD9(B $B>>:,!!1Q |
17:00$B!A(B 17:20 | R125 | $B6KDcG;EY$NM-5!J*J,2r$K$*$1$k8w?(G^H?1~FC@-(B ($B6eBg%P%$%*%"!<%/(B) $B!{(B($B@5(B)$BGr@P(B $BJ8=((B$B!&(B($B6e9)Bg>p9)(B) $B@P9u(B $BNQ;R(B$B!&(B($B:4@$J]9b@l(B) $B5\@n(B $BMN8w(B | Photocatalytic activity Very-low concentration UV intensity
| S-12 | 345 |
17:20$B!A(B 17:40 | R126 | $B2C=y<>K!$K$h$k6u5$>t2=$NFC@-(B ($B6eBg%P%$%*%"!<%/(B) ($B@5(B)$BGr@P(B $BJ8=((B$B!&(B$B!{(B($B@5(B)$BED:e(B $BD>$B!&(B($B6e9)Bg>p9)(B) $B1J;3(B $BM$0l(B$B!&(B($B%"%$%/%)!<%/(B) $BN)@P(B $B7{<#(B | Rapid air purification Gaseous ammonia Simultaneous humidification and dehumidification
| S-12 | 346 |
R$B2q>l(B $BBh(B2$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BHx>e!!70(B) |
9:00$B!A(B 9:20 | R201 | $BEE2r?eAG!&;@AG$rMQ$$$?2a;@2=?eAG$ND>@\9g@.(B ($BJ!=wBg?M4V4D6-(B) $B!{(B($B3X(B)$B@n8}(B $B?N;R(B$B!&(B$BA086(B $B>^;R(B$B!&(B($B@5(B)$BApJI(B $B9n8J(B | hydrogen peroxide electrolysis catalyst
| S-12 | 258 |
9:20$B!A(B 9:40 | R202 | $B?eMO@-%]%j%^! ($BL>9)Bg(B) $B!{(B($B@5(B)$BD9DE(B $BM:0lO:(B$B!&(B($B@5(B)$B2CF#(B $BDw?M(B$B!&(B($B@5(B)$BB?ED(B $BK-(B | Water-soluble polymer Electrolyte Kinetics
| S-12 | 733 |
9:40$B!A(B 10:00 | R203 | CO$B%W%i%:%^$K$h$k%+!<%\%s%J%N%U%!%$%P!<$NDc299g@.!=4pHD:`NA$*$h$S?(G^6bB0$N1F6A!=(B ($BEl9)BgM}9)(B) $B!{(B($B@5(B)$B?9(B $B?-2p(B$B!&(B$BJ!C+(B $B>;?.(B$B!&(B($B@5(B)$BNkLZ(B $B@5><(B | CO plasma carbon nanofiber low temperature synthesis
| S-12 | 896 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BD9DE!!M:0lO:(B) |
10:00$B!A(B 10:20 | R204 | $BD>N.%Q%k%9J|EE$rMQ$$$??eMO1UCfM-5!1vAG7O=|Ap:^$N%W%i%:%^J,2r(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$B2OLn(B $B9'9,(B$B!&(B($B3X(B)$BF#ED(B $BN4J8(B$B!&(B$B2+(B $BN)0](B$B!&(B($B@5(B)$B>>ED(B $B?N | Plasma decomposition Wastewater treatment Organic chloride
| S-12 | 292 |
10:20$B!A(B 10:40 | R205 | $B4u%,%9%W%i%:%^$rMQ$$$?C:2=?eAG$NE>49(B ($B@iMU9)Bg(B) $B!{(B($B3X(B)$BJ!2,(B $BBgJe(B$B!&(B($B3X(B)$BD9E:(B $B42(B$B!&(B($B@5(B)$B>.NS(B $B4p$B!&(B($B@5(B)$BHx>e(B $B70(B | microwave plasma dehydrogenation
| S-12 | 549 |
10:40$B!A(B 11:00 | R206 | $BM6EEBN%P%j%"J|EEH?1~4o$rMQ$$$?%G%#!<%<%kGS%,%9Cf$NC:AG7OHyN3;R$N=|5n(B (RITE) $B!{(B($B@5(B)$BIz8+(B $B@i?R(B$B!&(B$B4V=j(B $BOBI'(B$B!&(B($B@5(B)$BU-(B $B?eNI(B$B!&(B($B@5(B)$BF#2,(B $BM40l(B$B!&(B($B@5(B)$B;3ED(B $B6=0l(B | diesel exhaust particulate matter dielectric barrier discharge
| S-12 | 415 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B?9!!?-2p(B) |
11:00$B!A(B 11:20 | R207 | TiN-CVD$B$NAm3gH?1~$N%b%G%k2=$H%R!<%?!<%W%j%3!<%H%7%_%e%l!<%7%g%s(B ($BEl5~%(%l%/%H%m%s(B) $B!{@n>e(B $B2m?M(B$B!&(B($BEl5~%(%l%/%H%m%s(BAT) $B66K\(B $B5#(B$B!&(B($BEl5~%(%l%/%H%m%s(B) ($B@5(B)$BBtED(B $B0jIW(B | TiN TiCl4 Reaction model
| S-12 | 803 |
11:20$B!A(B 11:40 | R208 | GaAs$BA*Br(BMOVPE$B@.D9$K$*$1$kIT=cJ*E:2C%,%9$N1F6A(B ($BElBg9)(B) $B!{(B($B@5(B)$BAW(B $B3$@/(B$B!&(B($B@5(B)$B?y;3(B $B@5OB(B$B!&(B($BElBg@hC<8&(B) $BCfLn(B $B5A><(B$B!&(B($BElBg9)(B) ($B@5(B)$BAz3@(B $B9,9@(B | MOVPE CVD Selective Growth
| S-12 | 470 |
11:40$B!A(B 12:00 | R209 | $BA*Br@.D9$rMxMQ$7$?(BInP-MOVPE$B%W%m%;%9$N2r@O(B ($BElBg9)(B) $B!{(B($B3X(B)$B2&(B $B1>K2(B$B!&(B($B@5(B)$BAW(B $B3$@/(B$B!&(B($B@5(B)$B?y;3(B $B@5OB(B$B!&(B($BElBg@hC<8&(B) $BCfLn(B $B5A><(B$B!&(B($BElBg9)(B) ($B@5(B)$BAz3@(B $B9,9@(B | InP MOVPE Selective Growth
| S-12 | 474 |