SCEJ

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$B:G=*99?7F|;~!'(B2007-07-24 09:36:53
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(9:00$B!A(B10:40)$B!!(B($B:BD9(B $BD9C+It?-<#(BE$B1JED8g(B)
9:00$B!A(B 9:20B301[$BE8K>9V1i(B] S88$B%b%G%k$K4p$E$/%P%C%A%W%i%s%H$N
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ISA-S88 (IEC61512)
Batch control
Standard
S-11125
9:20$B!A(B 9:40B302$B2=3X%W%m%;%9$K$*$1$k@8;:7W2h%9%1%8%e!<%j%s%0%7%9%F%`$NE,MQ;vNc(B
($B;0I)2=3X%(%s%8%K%"%j%s%0(B) $B!{(B($B@5(B)$B?9;3(B $B>?(B
Scheduler
APS
Optimization
S-1510
9:40$B!A(B 10:00B303$B3,AX%P%C%A%W%m%;%9%b%G%k$rMxMQ$7$?1?E>7W2h$N:vDj(B
($BL>Bg9)(B) $B!{(B($B3X(B)$B66D^(B $B8g(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B
operation planning
hierarchical batch process model
discrete event system
S-1893
10:00$B!A(B 10:20B304$B%7%9%F%`7W2h!&1?E>$rBP>]$H$7$?0U;W7hDj;Y1g$N$?$a$N%b%G%j%s%0(B
($BL>Bg9)(B) $B!{(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B3X(B)$B>.L:(B $B=_J?(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B
decision making
system planning and operation
model standards of conduct
S-1897
10:20$B!A(B 10:40B305Optimal operating condition for specified molecular weight distribution in continuous free-radical polymerization
($BF`NI@hC$B!&(B($B@5(B)$BLnED(B $B8-(B$B!&(B($B@5(B)$B@>C+(B $B9I0l(B
Polymer quality control
molecular weight distribution
objective function
S-1802
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $B66K\K'9((BE$B;3Cf;KI'(B)
10:40$B!A(B 11:00B306[$BE8K>9V1i(B] $B%j%5%$%/%k%7%9%F%`$NHs@~7A@-$H:GE,2=@)8f(B
($BEl9)Bg;q8;8&(B) $B!{(B($B@5(B)$B4X(B $B9(Li(B
recycle systems
nonlinearities
process control
S-11128
11:00$B!A(B 11:20B307$B%j%"%k%?%$%`:GE,2=@)8f$HB?JQ?t%b%G%kM=B,$K$h$k@)Ls2sHr@)8f$H$N%O%$%V%j%C%I7?@)8f$NDs0F$HMQLr@_Hw$X$NE,MQ(B
($B=P8w6=;:(B) ($BIt(B)$BC+(B $BE/$B!&(B$B!{>>Hx(B $B9L;0(B
real-time optimization
closed loop control
energy system
S-1160
11:20$B!A(B 11:40B308$B2=3X9)3X
($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BCv;R(B $B42;J(B$B!&(B($B@5(B)$B>>K\(B $B=(9T(B$B!&(B($B@5(B)$B9uED(B $B@i=)(B
coaching
multiagent system
knowledge structure
S-159
11:40$B!A(B 12:00B309$B@EEE5$GK2u$rKI;_$9$kF3EE@-%0%i%9%i%$%K%s%0(B
($B?@9]4D6-%=%j%e!<%7%g%s(B) $B!{B?ED(B $BFF;V(B$B!&(B($B@5(B)$BA0GX8M(B $BCR@2(B$B!&(B$B5\Fb(B $B7$B!&(B$B9a@n(B $BGn9T(B
glass lining
ECO
static charge
S-1167
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $BDS?"5AJ8(BE$BF#_7Lw@8(B)
13:00$B!A(B 13:20B313[$BE8K>9V1i(B] Learning Algorithm for Trend Analysis and Fault Diagnosis
($B2,;3Bg(B) $B!{(B($B@5(B)A. Gabbar Hossam
Fault Diagnosis
Trend Analysis
Operation Design
S-11129
13:20$B!A(B 13:40B314[$BE8K>9V1i(B] EEMUA$B%,%$%I%i%$%s$K$_$k%W%i%s%H%"%i!<%`%7%9%F%`$N@_7W$HI>2A(B
($BF`NI@hC
EEMUA
Alarm System Design
Virtual Subject
S-11127
13:40$B!A(B 14:00B315$B%W%i%s%H%7%_%e%l!<%?$K$h$k1?E>3W?7(B
($B%*%a%,%7%_%e%l!<%7%g%s(B) $B!{(B($B@5(B)$B2#;3(B $B9n8J(B$B!&(B($B%?%$%K!<%^%&%9(B) ($B@5(B)$B>.8}(B $B8hO:(B$B!&(B($B%*%a%,%7%_%e%l!<%7%g%s(B) $B@nB<(B $B7QIW(B$B!&(B($B2#2OEE5!(B) $BBgC+(B $BE/Li(B
online simulation
plant visualization
parameter identification
S-1770
14:00$B!A(B 14:20B316$B%H%i%C%-%s%0%7%_%e%l!<%?$K$h$k%a%?%s?e>x5$2~>r7o;;=P(B
($B2#2OEE5!(B) $B!{(B($B@5(B)$BHx>e(B $BG+(B$B!&(B$B2O8}(B $B63FsO:(B$B!&(B$BCgLp(B $B$B!&(B$BBgC+(B $BE/Li(B
Tracking simulator
Steady-state prediction
Methane steam reformer
S-1321
(14:20$B!A(B15:40)$B!!(B($B:BD9(B $B;32
14:20$B!A(B 14:40B317$BFHN)@.J,J,@O$rMQ$$$??75,%=%U%H%;%s%5!<
($BElBg1!9)(B) ($B3X(B)$B6b;R(B $B90>;(B$B!&(B$B!{(B($B@5(B)$B9S@n(B $B@544(B$B!&(B($B@5(B)$BA%DE(B $B8x?M(B
soft sensor
independent component analysis
process control
S-1449
14:40$B!A(B 15:00B318$B%^%$%/%m%j%"%/%?$N%;%s%5G[CV$H>uBV?dDj(B
($B5~Bg9)(B) ($B3X(B)$B1J86(B $BAo;N(B$B!&(B$B!{(B($B@5(B)$BEBB<(B $B=$(B$B!&(B($B@5(B)$B2CG<(B $B3X(B$B!&(B($B@5(B)$BD9C+It(B $B?-<#(B
microreactor
sensor location
state estimation
S-1733
15:00$B!A(B 15:20B319[$BE8K>9V1i(B] $BJ#?t$N%9%3!<%W$K4p$E$/%W%m%;%9%b%K%?%j%s%0$X$NCNE*%7%9%F%`%:%"%W%m!<%A(B
($BEl9)Bg1!M}9)(B) $B!{(B($B@5(B)$B>>K\(B $B=(9T(B
Process monitoring
Intelligent system
S-11126
15:20$B!A(B 15:40_

$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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