SCEJ

$B2=3X9)3X2q(B $BBh(B74$BG/2q(B($B2#IM(B)

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$B%7%9%F%`!&>pJs!&%7%_%e%l!<%7%g%s(B

D302-D320

$B:G=*99?7F|;~!'(B2009-03-11 14:01:08
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
D$B2q>l(B $BBh(B3$BF|(B
(9:20$B!A(B10:00)$B!!(B($B:BD9(B $BC+8}(B $BCR(B)
9:20$B!A(B 9:40D302$B%W%m%;%9@_7W5Z$S2=3XJ*2A$K4X$9$kCN<1$N9=B$2=(B-$B6bB0@v>t%W%m%;%9$X$NE,MQ(B
($BElBg9)(B) $B!{(B($B3X(B)$B5FCS(B $B9/5*(B$B!&(B($B@5(B)$BJ?Hx(B $B2mI'(B		Industrial cleaning
Activity modeling
Information modeling
6-f430
9:40$B!A(B 10:00D303$B@v>t:^GS=PM^@)$N$?$a$NBeBX@v>t%W%m%;%90FF3=P%7%9%F%`$N
($BElBg9)(B) $B!{(B($B3X(B)$BLZB<(B $BM}0lO:(B$B!&(B($B3X(B)$B5FCS(B $B9/5*(B$B!&(B($B@5(B)$BJ?Hx(B $B2mI'(B		Industrial Cleaning
Engineering Knowledge
Process Design
6-g448
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B2CG
10:00$B!A(B 10:20D304Structural Framework Supporting Multi-objective Selection of Extraction Processes
(The U. Tokyo) $B!{(B($B3X(B)Nguyen Thuy$B!&(B(ETH Zurich) Sugiyama Hirokazu$B!&(B(Nara Inst. Sci. and Tech.) ($B@5(B)Noda Masaru$B!&(B(The U. Tokyo) ($B@5(B)Hirao Masahiko		structural framework
extraction processes
multi-objective optimization
6-b270
10:20$B!A(B 10:40D305$B%3%W%m%@%/%7%g%s%T%s%A2r@O%D!<%k$rMQ$$$?<+8JG.:F@87?%W%m%;%9$NI>2A(B
($B;:Am8&(B) $B!{(B($B@5(B)$BC+8}(B $BCR(B$B!&(B($B@5(B)$BCf4d(B $B>!(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B$B!&(B($B%7%`%F%C%/(B) ($B@5(B)$BC'(B $B9@G7(B		CoProduction system
pinch analysis
energy saving
6-b14
10:40$B!A(B 11:00D306$BCJEc7?(BHIDiC$B$NEAG.%b%G%k(B
($BL>9)Bg(B) $B!{(B($B3X(B)$BEOIt(B $BCR4p(B$B!&(B($B@5(B)$BB9(B $B9HG_(B$B!&(B($B@5(B)$B66K\(B $BK'9((B		Distillation
Energy Conservation
Heat Integration
6-b303
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BLnED!!8-(B)
11:00$B!A(B 11:20D307QSPR$B%b%G%k$NE,MQHO0O$rDj$a$k$?$a$NHFMQE*$J
($BElBg1!9)(B) $B!{(B($B3X(B)$B1&ED(B $B7<:H(B$B!&(B($B@5(B)$B9S@n(B $B@544(B$B!&(B($B@5(B)$BA%DE(B $B8x?M(B		QSPR
AD(Applicability Domain)
Chemometrics
6-g317
11:20$B!A(B 11:40D308$B%]%j%^!<%W%i%s%H$K$*$1$k%H%i%s%8%7%g%s=*N;H=Dj%b%G%k$N9=C[$H%=%U%H%;%s%5!<$X$N1~MQ(B
($BElBg1!9)(B) $B!{(B($B3X(B)$B6b;R(B $B90>;(B$B!&(B($B@5(B)$B9S@n(B $B@544(B$B!&(B($B@5(B)$BA%DE(B $B8x?M(B		soft sensor
transition
process control
6-d13
11:40$B!A(B 12:00D309$BA`6H%G!<%?$+$i$N%W%i%s%HF1Dj$K4X$9$k9M;!(B-$B@~7A4X?t%b%G%k$K$h$k%"%W%m!<%A(B-
($BL>9)Bg(B) $B!{(B($B3X(B)$B;38}(B $B@.H~(B$B!&(B($B@5(B)$BJFC+(B $B>$B!&(B($B%A%N!<(B) $B@P66(B $B@/;0(B		plant identification
process control
plant model
6-d104
12:00$B!A(B 13:00$BCk5Y$_(B
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B9S@n(B $B@544(B)
13:00$B!A(B 13:20D313TCM:$B%H!<%?%k%3%9%H%^%M%8%a%s%H(B-$B%W%m%8%'%/%H!&%9%3!<%W$H
($B%3%9%H9)3X8&(B) $B!{(B($B@5(B)$Bc7F#(B $B5A8J(B		Total Cost Management
Project Scope
Work Breakdown Structure
6-a355
13:20$B!A(B 13:40D314$BIT3NDj<{MW2<$G$NB?IJ
($B5~Bg9)(B) $B!{(B($B@5(B)$BD9C+It(B $B?-<#(B$B!&(B$BDT(B $BM*M$(B$B!&(B($B@5(B)$B2CG<(B $B3X(B		Demand uncertainty
Production planning
Inventory planning
6-a470
13:40$B!A(B 14:00D315$B4D6-JQ2=$r9MN8$7$?0U;W7hDj;Y1g$N$?$a$N%b%G%j%s%0(B
($BL>Bg9)(B) $B!{(B($B3X(B)$B>.L:(B $B=_J?(B$B!&(B($B3X(B)$B]/0f(B $B7=Je(B$B!&(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B		decision making support
modeling
environmental change
6-a432
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B>>K\!!=(9T(B)
14:00$B!A(B 14:20D316$BDj@-%b%G%k$rMxMQ$7$?%P%C%A%W%m%;%9$N0[>o?GCG(B
($BL>Bg9)(B) $B!{(B($B3X(B)$B7-2<(B $BM%5.;R(B$B!&(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B		fault diagnosis
qualitative model
batch process
6-a431
14:20$B!A(B 14:40D317Cause-Effect$B%b%G%k$K4p$E$/%"%i!<%`%7%9%F%`$N@_7W(B
($B@EBg9)(B) $B!{(B($B3X(B)$BBg@>(B $BCR;N(B$B!&(B($B@5(B)$BIpED(B $BOB9((B$B!&(B($BL>9)Bg(B) ($B@5(B)$BIM8}(B $B9';J(B$B!&(B($B6eBg9)(B) ($B@5(B)$BLZB<(B $BD>$B!&(B($BF`NI@hC		Cause-Effect Model
Alarm System
Design
6-a91
14:40$B!A(B 15:00D318$B%^%$%/%m2=3X%W%m%;%9$NJD:I%A%c%M%k8!=P$HJD:IN(?dDj(B
($BF`NI@hC$B!&(B($B@5(B)$BLnED(B $B8-(B$B!&(B($B@5(B)$B@>C+(B $B9I0l(B		microreactor
channel blockage
fault diagnosis
6-a171
(15:00$B!A(B15:40)$B!!(B($B:BD9(B $B66D^!!?J(B)
15:00$B!A(B 15:20D319Optimal Grade Transition in Continuous Polymerization Reactor
($BF`NI@hC$B!&(B($B@5(B)$BLnED(B $B8-(B$B!&(B($B@5(B)$B@>C+(B $B9I0l(B		Dynamic optimization
Grade transition
Polymer quality control
6-e513
15:20$B!A(B 15:40D320$BIT0BDj@-$rH<$&N.BN%7%9%F%`$K$*$1$k?6F0%Q%?!<%s$N%^%k%A%9%1!<%k2r@O(B
($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BF#2,(B $B:;ET;R(B$B!&(B($B@5(B)$B>>K\(B $B=(9T(B$B!&(B($B@5(B)$B9uED(B $B@i=)(B		exothermic reaction
oscillatory phenomenon
multiscale analysis
6-c62
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B74$BG/2q(B($B2#IM(B)
(C) 2009 ($B
Most recent update: 2009-03-11 14:01:08
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