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$BH?1~9)3X(B |
(9:30$B!A(B10:42) ($B:BD9(B $B>.NS(B $BBgM4!&Fs5\(B $B9R(B) |
9:30$B!A(B 9:42 | C01 | SiCf/SiC-CMC $B@=B$MQ2=3X5$Aj4^?/(B(CVI)$BK!$NA!0]B+4V9bB.Kd$a9~$_>r7o$N8!F$(B
($BElBg9)(B) $B!{LZB<(B $B=S2p(B$B!&(B ($BElBg1!9)(B) ($B3X(B)$BBg|b(B $BM:J?(B$B!&(B ($B@5(B)$B:4F#(B $BEP(B$B!&(B (IHI) ($B@5(B)$BJ!Eg(B $B9/G7(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$B=P1:(B $BEm;R(B$B!&(B ($B@5(B)$BI4@%(B $B7r(B$B!&(B ($B@5(B)$BAz3@(B $B9,9@(B | SiC CVI CVD
| 5-h | 98 |
9:42$B!A(B 9:54 | C02 | ALD$B$rMQ$$$?(BCo$BGvKl@.D9$K$*$1$kI=LL=hM}8z2L$N8!F$(B
($BElBg(B) $B!{;3yu(B $B=YJe(B$B!&(B ($B3X(B)$B;38}(B $B=a(B$B!&(B ($B@5(B)$B:4F#(B $BEP(B$B!&(B ($B@5(B)$B=P1:(B $BEm;R(B$B!&(B ($B@5(B)$BI4@%(B $B7r(B$B!&(B ($B@5(B)$BAz3@(B $B9,9@(B | AS-ALD surface treatment ULSI
| 5-h | 258 |
9:54$B!A(B 10:06 | C03 | $B%a%?%sG.J,2r?eAG@=B$AuCV$K$*$1$k?eAG%P!<%J$N8!F$(B
($B4tIlBg(B) $B!{>e86(B $BBsKa(B$B!&(B ($B3X(B)$BIpF#(B $BCRBg(B$B!&(B ($B@5(B)$BD+86(B $B@?(B$B!&(B $B5\:d(B $BIp;V(B$B!&(B ($BElBg(B) $B1[(B $B8wCK(B | Hydrogen Methane pyrolysis Burner
| 3-b | 230 |
10:06$B!A(B 10:18 | C04 | $BFsN.BN%b%G%k$K$h$k5$8GH?1~AuCV$N%7%_%e%l!<%7%g%s(B
($B:k6LBg9)(B) $B!{5\2<(B $BBg6u(B$B!&(B ($B:k6LBg1!(B) ($B3X(B)$B@iMU(B $B9/B@O:(B$B!&(B ($B@5(B)$BK\4V(B $B=S;J(B | two-fluid model Gas-Solid reaction fluorination of uranium dioxide
| 2-a | 276 |
10:18$B!A(B 10:30 | C05 | $B7\J5>F5Q3%$+$i%j%s$N2s<}$KBP$9$k%9%1!<%k%"%C%W$N1F6A(B
($BFAEgBgM}9)(B) $B!{66K\(B $BBs3$(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | phosphorus recovery chicken manure scale-up
| 5-g | 14 |
10:30$B!A(B 10:42 | C06 | $B2F5Q3%$+$i$N%j%s$N2s<}(B
($BFAEgBgM}9)(B) $B!{1)86(B $B>-5.(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B$B!&(B ($B5OC[5;=Q;N;vL3=j(B) $B0$It(B $B@60l(B | phosphorus recovery sewage sludge acid-alkaline treatment
| 5-g | 15 |
10:42$B!A(B 10:50 | $B5Y7F(B |
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(10:50$B!A(B12:02) ($B:BD9(B $B:4F#(B $B9d;K!&I4@%(B $B7r(B) |
10:50$B!A(B 11:02 | C08 | $B%(%"%P%C%0MQ%,%9H/@8:^$H$7$F$N(B1H-$B%H%j%"%>!<%kF<:xBN$NG.0BDj@-$H5[<>@-(B
($BJ!2,Bg9)2=3X%7%9%F%`9)3X2J(B) $B?@:j(B $B:nLo(B$B!&(B $B!{>.Eg(B $BM%$B!&(B ($B@5(B)$B=E>>(B $B44Fs(B$B!&(B ($B@5(B)$B%3%&%O%/%k(B $B%o%5%J(B | Thermal stability Hygroscopicity Azole
| 3-f | 236 |
11:02$B!A(B 11:14 | C09 | $B@8@.J*$NJ,N%$r2sHr$9$k(B2-$B%/%m%m%W%m%Z%s$NA*BrE*@\?(4T85(B
($BFAEgBgM}9)(B) $B!{2,K\(B $B0!9aN$(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | selective catalytic reduction 2-chloropropene propylene
| 5-a | 16 |
11:14$B!A(B 11:26 | C10 | $B%W%m%Q%s$N4^;@AG2=9gJ*$X$N@\?(JQ49(B
($BFAEgBgM}9)(B) $B!{@>B<(B $BB@0l(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | catalytic conversion propane oxygen-containing compounds
| 5-a | 13 |
11:26$B!A(B 11:38 | C11 | $B%"%k%_%JC4;};@2=%K%C%1%k?(G^$K$h$k%(%?%s$NC&?eAG(B
($BFAEgBgM}9)(B) $B!{4d>k(B $B97>0(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B$B!&(B ($B;0I)%1%_%+%k(B) ($B@5(B)$B2CF#(B $BM5$B!&(B ($B@5(B)$BFs5\(B $B9R(B | dehydrogenation ethane nickel oxide
| 5-a | 84 |
11:38$B!A(B 11:50 | C12 | BCN$B:`NA$ND4@=$H$=$N1v4p?(G^3h@-I>2A(B
($B72BgM}9)(B) $B!{@>_7(B $B7E(B$B!&(B ($B72Bg1!M}9)(B) ($B@5(B)$B?@@.(B $B>09n(B$B!&(B ($B@5(B)$B:4F#(B $BOB9%(B | Heterogeneous catalyst Base catalyst Knoevenagel reaction
| 5-a | 305 |
11:50$B!A(B 12:02 | C13 | Ni-Cu$BC4;}3h@-C:%/%m%9$K$h$k%a%?%N!<%k?eMO1U2~
($BEl5~EE5!Bg(B) $B!{F|CV(B $B>OB@(B$B!&(B ($B@5(B)$B>.NS(B $BBgM4(B | Ni-Cu catalyst Hydrogen Reforming
| 5-a | 176 |
12:02$B!A(B 12:14 | $BCk5Y$_(B |
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13:00$B!A(B 13:12 | C19 | $B%U%'%N!<%k$ND62;GHJ,2r$K<~GH?t$,$*$h$\$91F6A(B
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| 5-b | 157 |
13:12$B!A(B 13:24 | C20 | $BD62;GH$K$h$k%(%^%k%7%g%sD4@=$H%]%j%9%A%l%s9g@.(B
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| 5-b | 161 |
13:24$B!A(B 13:36 | C21 | $B%^%$%/%m<><0KB;e%G%P%$%9$NN.O)9=B$$,(BJet$BN.$N0BDj@-$K5Z$\$91F6A(B
($B2,;3Bg9)(B) $B!{Kv8w(B $B@;(B$B!&(B ($B2,;3Bg1!<+(B) ($B3X(B)$B??Fi(B $BNP(B$B!&(B ($B@5(B)$BEOn4(B $B5.0l(B$B!&(B ($B@5(B)$B>.Ln(B $BEX(B | Computational fluid dynamics Jet flow Microfluidics
| 5-f | 104 |
13:36$B!A(B 13:48 | C22 | $BFs;@2=C:AG;q8;2=MQ$N?75,KlH?1~4o3+H/(B
($B$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B | Membrane Reactor Carbon neutral Methanation
| 5-d | 61 |
13:48$B!A(B 14:00 | C23 | Dushman$BH?1~$NH?1~B.EY$K1v$,5Z$\$91F6A$N2r@O(B
($BElM}Bg(B) $B!{;3_7(B $B=(B@(B$B!&(B ($B@5(B)$BB<>e(B $BM5:H(B$B!&(B ($B@5(B)$B>>@n(B $BGnN<(B$B!&(B ($B@5(B)$BBgC](B $B>!?M(B$B!&(B ($B@5(B)$B>1Ln(B $B8|(B | Dushman reaction kinetic study reaction engineering
| 5-f | 283 |
14:00$B!A(B 14:12 | C24 | $B?eAGF)2aKlEE6K$rMQ$$$??eEE2rAuCV$N2~NI(B
($B1'ET5\Bg9)(B) ($B@l(B4)$B!{;3Cf(B $B@151(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD> | electrolysis of water hydrogen production hydrogen permeable membrane
| 5-e | 122 |
14:12$B!A(B 14:20 | $B5Y7F(B |