SCEJ

$B2=3X9)3X2q(B $BBh(B39$B2s=)5(Bg2q(B

$B9V1i%W%m%0%i%`!J2q>l!&F|DxJL!K(B

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$B:G=*99?7F|;~!'(B2007-07-24 09:36:53
$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 $B!c29CH2=BP:v$rC4$&>xN15;=Q(B-$B%b%G%j%s%0$+$i%W%m%;%91?E>$^$G!d(B
(9:00$B!A(B9:40)$B!!(B($B;J2q(B $B>.?{?M;|(B)
9:00$B!A(B 9:40B101[$BE8K>9V1i(B] $B%W%m%;%9A4BN$rPmbW$7$?>J;q8;!&>J%(%M%k%.!<$N
($B=P8w6=;:(B) $B!{(B($B@5(B)$BEDB<(B $B7		resource saving
energy saving
process design and operation
S-181106
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $B>>ED7=8g(B)
9:40$B!A(B 10:00B103$BFbItG.8r49>xN1Ec(B(HIDiC)$B$N5sF0(B
($BElM}Bg9)(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B		HIDiC
distillation
energy saving
S-18214
10:00$B!A(B 10:20B104$BFbItG.8r497?>xN1Ec(B(HIDiC)$B$NIi2YJQF01?E>$N7k2L$K$D$$$F(B
($B4]A1@PL}2=3X(B) $B!{(B($B@5(B)$BKYFb(B $B6QJ?(B$B!&(B($B@5(B)$B0fFb(B $B8,Je(B$B!&(B($B4X@>2=3X(B) ($B@5(B)$BJR2,(B $BK.IW(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B		HIDiC
Distillation
Energy Saving
S-18322
10:20$B!A(B 10:40B105$B%W%l!<%H%U%#%s7?(BHIDiC$B$K$h$k6u5$J,N%
($BBgM[F|;@(B) $B!{(B($B@5(B)$B9>1[(B $B?.L@(B$B!&(B$B@P@n(B $B0l=S(B$B!&(B$B:d>e(B $B@?0l(B$B!&(B($B@5(B)$B@n>e(B $B9@(B		HIDiC
cryogenic distillation
air separation
S-181032
10:40$B!A(B 11:00B106HIDiC$B2=:GE,%"%W%j%1!<%7%g%sA*Dj$H$=$N5;=QGX7J(B
($BElMN%(%s%8(B) ($B@5(B)$B_@B<(B $B8wMx(B$B!&(B$B!{$B!&(B$B6L1[(B $B>		Column Grand Composite Curve
Component Pinch
Energy Saving
S-181102
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B4dJI9,;T(B)
11:00$B!A(B 11:20B107Compressorless HIDiC$B%7%9%F%`$N2DG=@-(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)$BARC+(B $B?-9T(B$B!&(B($B@5(B)$B8~ED(B $BCi90(B$B!&(B($B@5(B)$B6bED(B $BK|J?(B$B!&(B($B4]A1@PL}(B) ($B@5(B)$BKYFb(B $B6QJ?(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B		Multi-component distillation
Energy saving
Compressorless HIDiC
S-1811
11:20$B!A(B 11:40B108$BBg8}7B(BHIDiC$B$N
($BLZB<2=9)(B) $B!{(B($BIt(B)$BCf@>(B $B=S@.(B$B!&(B$BB-N)(B $B>0fb(B$B!&(B($BIt(B)$B0$A>(B $B0l@5(B$B!&(B($B;:Am8&(B) ($BIt(B)$BCf4d(B $B>!(B$B!&(B($B;37ABg(B) ($BIt(B)$B>>ED(B $B7=8g(B$B!&(B($BLZB<2=9)(B) $B9b>>(B $BIp0lO:(B		HIDiC
Distillation
Experiment
S-18711
11:40$B!A(B 12:00B109$BBg8}7B(BHIDiC$B$N%7%_%e%l!<%7%g%s%b%G%k$N8!F$(B
($BLZB<2=9)(B) $B!{B-N)(B $B>0fb(B$B!&(B($BIt(B)$BCf@>(B $B=S@.(B$B!&(B($BIt(B)$B0$A>(B $B0l@5(B$B!&(B($B;:Am8&(B) ($BIt(B)$BCf4d(B $B>!(B$B!&(B($B;37ABg(B) ($BIt(B)$B>>ED(B $B7=8g(B$B!&(B($BLZB<2=9)(B) $B9b>>(B $BIp0lO:(B		HIDiC
Distillation
Simulation
S-18722
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $BCf4d(B $B>!(B)
13:00$B!A(B 13:40B113[$B>7BT9V1i(B] Energy Saving by Heat Integration in Distillation Process
($BKL5~2=9)Bg(B) $B!{(B($B@5(B)$B2+(B $B9n6`(B		energy saving
heat integration
control
S-18631
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $B?9(B $B=(
13:40$B!A(B 14:00B115$BFbItG.8r497?>xN1Ec$N9=B$$*$h$S1?E>$HB?=EDj>o>uBV(B
($B5~Bg9)(B) $B!{(B($B3X(B)$B4,ED(B $B9@(B$B!&(B($B@5(B)$B2CG<(B $B3X(B$B!&(B($B@5(B)$BD9C+It(B $B?-<#(B		heat integrated distillation column
multiple steady states
operation and control
S-1850
14:00$B!A(B 14:20B116HIDiC$B%7%9%F%`$N(BgPROMS$B$K$h$k%b%G%j%s%0(B
($B%T!<%(%9%$!<%8%c%Q%s(B) $B!{(B($B@5(B)$BGp20(B $B<"(B		modeling
exergy analysis
HIDiC
S-18603
14:20$B!A(B 14:40B117$B%W%l!<%H7?G.8r494o9=B$$rM-$9$k(BHIDiC$B$K$h$k%W%m%;%96/2=(B
($B;37ABg1!M}9)(B) $B!{(B($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B;:Am8&(B) ($B@5(B)$B4dJI(B $B9,;T(B$B!&(B($B@5(B)$BCf4d(B $B>!(B		plate heat exchanger
heat integration
process intensification
S-1824
(14:40$B!A(B15:40)$B!!(B($B:BD9(B $B9>1[?.L@(B)
14:40$B!A(B 15:00B118$BFbItG.8r497?>xN1Ec(B(HIDiC)$B$K$*$1$kJ*
(E&E$B%W%i%K%s%0(B) $B!{(B($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)$BCf4d(B $B>!(B$B!&(B($B;0I)2=3X(B) $B5WJ](B $BOBLi(B$B!&(B$BKY8}(B $B>=IW(B$B!&(B($B;:Am8&(B) ($B@5(B)$B;3K\(B $BBs;J(B$B!&(B($B@5(B)$BJR2,(B $B>M(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B		HIDiC
distillation
heat transfer
S-18539
15:00$B!A(B 15:20B119$BB.EYO@%b%G%k$K4p$E$/FbItG.8r497?>xN1Ec(BHIDiC$B$N2r@O(B
($BL>9)Bg(B) $B!{(B($B3X(B)$BA0ED(B $BCRMN(B$B!&(B($B@5(B)$B?9(B $B=($B!&(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B7		HIDiC
Distillation
Rate based model
S-18729
15:20$B!A(B 15:40B120$B
($BL>9)Bg(B) ($B@5(B)$B?9(B $B=($B!&(B$B!{(B($B3X(B)$B9CHe(B $B=V(B$B!&(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B7		Rate based model
Vapor/Liquid contacting
Device Simulation
S-18732
(15:40$B!A(B16:40)$B!!(B($B:BD9(B $B_@B<8wMx(B)
15:40$B!A(B 16:00B121$BH?1~>xN1%W%m%;%9$NB.EYO@%b%G%k$K$h$k2r@O(B
($BL>9)Bg(B) ($B@5(B)$B?9(B $B=($B!&(B$B!{(B($B3X(B)$BEgED(B $BBgJe(B$B!&(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B7$B!&(B($B;0I)2=9)5!(B) $BLn:d(B $B4p(B		Reactive Distillation
Rate Based Model
Simulation
S-18739
16:00$B!A(B 16:20B122$B>xN1(B-$BJ,N%Kl%O%$%V%j%C%I%W%m%;%9$K$h$kB?@.J,7OJ,N%(B
($BEl9)BgM}9)(B) $B!{(B($B@5(B)$B>.?{(B $B?M;|(B$B!&(B($BEl9)Bg9)(B) ($B3X(B)$B0$It(B $B9@G7(B		Simulation
distillation
membrane
S-181048
16:20$B!A(B 16:40B123$BD60!NW3&%W%m%Q%s$K$h$k%P%$%*%(%?%N!<%k$N>J%(%MC&?e%W%m%;%9$N:GE,2=(B($B$=$N(B2)
($BL>Bg1!9)(B) $B!{(B($B3X(B)$BBg5WJ](B $B7D0l(B$B!&(B($B@5(B)$B0BED(B $B7<;J(B$B!&(B($B@5(B)$BKYE:(B $B9@=S(B		Supercritical Extraction
Dehydration
Ethanol
S-1894
(16:40$B!A(B17:20)$B!!(B($B:BD9(B $B>.?{?M;|(BE$B4dJI9,;T(BE$B>>ED7=8g(B)
16:40$B!A(B 17:00_
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B39$B2s=)5(Bg2q(B
(C) 2007 ($B
Most recent update: 2007-07-24 09:36:53
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