$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B |
$B%7%s%]%8%&%`(B $B!cJ,N%%W%m%;%9It2q%7%s%]%8%&%`!d(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B4dJI(B $B9,;T(B) |
9:00$B!A(B 9:20 | V201 | $BB.EYO@%b%G%k$rMQ$$$??bD>J,3d7?>xN1%W%m%;%9$NA`:nFC@-$N9M;!(B ($BL>9)Bg(B) $B!{(B($B3X(B)$B9l(B $B>05*(B$B!&(B($B3X(B)$BA0ED(B $BCRMN(B$B!&(B($B7$B!&(B($BL>9)Bg(B) ($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B@5(B)$B?9(B $B=( | Distillation Dividing Wall Column Rate-based model
| S-10 | 749 |
9:20$B!A(B 9:40 | V202 | $BFbItG.8r497?>xEc$N5sF0(B ($BElM}Bg(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | HIDiC saving energy distillation
| S-10 | 798 |
9:40$B!A(B 10:00 | V203 | $BFbItG.8r497?>xN1Ec$N>J%(%M%k%.!<@-$H4D6-@-$NI>2A(B ($B;37ABg1!M}9)(B) $B!{(B($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B4]A1%F%/%N%5!<%S%9(B) ($B@5(B)$BKYFb(B $B6QJ?(B$B!&(B($B;:Am8&(B) ($B@5(B)$B4dJI(B $B9,;T(B$B!&(B($BElBg@88&(B) ($B@5(B)$BCSED(B $B2m90(B$B!&(B($BLZB<2=9)5!(B) ($B@5(B)$BCf@>(B $B=S@.(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B | energy-saving distillation greenhouse gas mitigation cyclopentane purification
| S-10 | 810 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BBg9>(B $B=$B$(B) |
10:00$B!A(B 10:20 | V204 | $BFbItG.8r497?>xN1Ec(B(HIDiC)$B$K$*$1$k>J%(%M%k%.!<2r@O(B ($BElBg@88&(B) $B!{(B($B@5(B)$BCSED(B $B2m90(B$B!&(B($B;:Am8&(B) ($B@5(B)$B4dJI(B $B9,;T(B$B!&(B($B;37ABg1!M}9)(B) ($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B;:Am8&(B) ($B@5(B)$BC+8}(B $BCR(B$B!&(B($B@5(B)$BJR2,(B $B>M(B$B!&(B($B@5(B)$B;3K\(B $BBs;J(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B$B!&(B($B@5(B)$BCf4d(B $B>!(B | HIDiC Energy saving Simulation
| S-10 | 880 |
10:20$B!A(B 10:40 | V205 | $B05=L5!$rI,MW$H$7$J$$8:057O(BHIDiC$B$NE,MQ@-$N2r@O(B ($B4X@>2=3X(B) ($B@5(B)$BLnED(B $B=(IW(B$B!&(B$B!{(B($B@5(B)$BJR2,(B $BK.IW(B$B!&(B($B@5(B)$B;3O)(B $B42;J(B$B!&(B($B@5(B)$B6bED(B $BK|J?(B$B!&(B($B@5(B)$B8~ED(B $BCi90(B$B!&(B($B@5(B)$BARC+(B $B?-9T(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B | Distillation Compressor-free HIDiC
| S-10 | 8 |
10:40$B!A(B 11:00 | V206 | $BFbItG.8r497?>xN1Ec(B(HIDiC)$B%Q%$%m%C%H%W%i%s%H$N1?E>2r@O$H%7%_%e%l!<%7%g%s(B ($B;:Am8&(B) $B!{(B($B@5(B)$B4dJI(B $B9,;T(B$B!&(B($B4]A1%F%/%N%5!<%S%9(B) ($B@5(B)$BKYFb(B $B6QJ?(B$B!&(B($BLZB<2=9)5!(B) ($B@5(B)$BCf@>(B $B=S@.(B$B!&(B($B;37ABg1!M}9)(B) ($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($BElBg@88&(B) ($B@5(B)$BCSED(B $B2m90(B$B!&(B($B;:Am8&(B) ($B@5(B)$BC+8}(B $BCR(B$B!&(B($B@5(B)$BJR2,(B $B>M(B$B!&(B($B@5(B)$B;3K\(B $BBs;J(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B$B!&(B($B@5(B)$BCf4d(B $B>!(B | heat integration overall heat transfer coefficient energy saving
| S-10 | 768 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B>>ED(B $B7=8g(B) |
11:00$B!A(B 11:20 | V207 | $B= ($BLZB<2=9)5!(B) $B!{B-N)(B $B>0fb(B$B!&(B($B@5(B)$BCf@>(B $B=S@.(B | HIDiC Distillation Structured Packing
| S-10 | 445 |
11:20$B!A(B 11:40 | V208 | $B= ($BElM}Bg(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | packed tower flooding point distillation
| S-10 | 806 |
11:40$B!A(B 12:00 | V209 | $BH?1~>xN1Ec$KBP$9$k2r@O%b%G%k$N8!F$(B ($BL>9)Bg(B) $B!{(B($B3X(B)$BJ?0f(B $B?-6F(B$B!&(B($B3X(B)$BEgED(B $BBgJe(B$B!&(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B@5(B)$B?9(B $B=($B!&(B($B7 | Reactive Distillation Kinetic Model Heat Mass Transfer Model
| S-10 | 740 |
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $B>.?{(B $B?M;|(B) |
13:00$B!A(B 13:20 | V213 | $BD62;GHL82=J,N%AuCV$K$*$1$k1?E>%(%M%k%.!<$N:G>.2=(B ($BL82=J,N%8&(B) $B!{(B($B@5(B)$B>>1:(B $B0lM:(B$B!&(B$B?$B!&(B$B0$It(B $BK< | $BD62;GHL82=(B $BJ,N%(B $B%(%?%N!<%k(B
| S-10 | 884 |
13:20$B!A(B 13:40 | V214 | $B%U%'%K%k%[%&;@$H(B4$B5i%"%s%b%K%&%`1v$K$h$k%8%*!<%kN`$NCj=P(B ($BF1;V>K\(B $BF;L@(B$B!&(B$BGrLZ(B $BN49%(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B | Extraction Diols Phenylborate
| S-10 | 129 |
13:40$B!A(B 14:00 | V215 | $B%3!<%k%?!<%k5[<}L}$NCj=PJ,N%(B-$B>xN1$K$h$kCj=PAj$NJ,N%$KBP$9$kCj=P>r7o$N1F6A(B- ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$B5HB<(B $B9n5W(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | Absorption oil Solvent extraction Distillation
| S-10 | 376 |
14:00$B!A(B 14:20 | V216 | $B%3!<%k%?!<%k5[<}L}$NF}2=1UKlJ,N%$KBP$9$kF)2aB%?J(B ($BEl9)BgM}9)(B) $B!{(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B3X(B)$BI-(B $BFA6b(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | coal tar absorption oil liquid-liquid equilibrium emulsion liquid membrane separation
| S-10 | 380 |
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $B9>F,(B $BN50l(B) |
14:20$B!A(B 14:40 | V217 | $B%[%?%F%,%$2C9)GQ4~J*$+$i$N%+%I%_%&%`=|5n$H@8J*J,2r@-6E=8:^$X$NMxMQ(B ($BKLBg1!?e(B) $B!{0K7n(B $BD>=((B$B!&(B($B@5(B)$B4X(B $B=(;J(B$B!&(B($B@5(B)$B4];3(B $B1QCK(B$B!&(B($B4D6-Am8&(B) $B@nJU(B $B2m@8(B$B!&(B$BCf=P(B $B?.Hf?M(B | Scollop waste Cadmium removal Competitive adsorption
| S-10 | 62 |
14:40$B!A(B 15:00 | V218 | $B$b$_3LC:$K$h$k>K;@%$%*%s$N5[CeJ,N%(B ($BEl9)Bg1!M}9)(B) $B!{(B($B@5(B)$B>.?{(B $B?M;|(B$B!&(B$BGpB<(B $BJ~I'(B$B!&(BEspiritu Rosana | adsorption rice hask
| S-10 | 990 |
15:00$B!A(B 15:20 | V219 | $B%5%s%I%&%#%C%A%/%m%^%H%0%i%U%#! ($B?@F`@n9)Bg(B) $B!{(B($B@5(B)$BBgDm(B $BIpBY(B$B!&(B$B?y;3(B $B;J(B$B!&(B$B?7B<(B $B8- | HPLC sandwich recycling
| S-10 | 930 |