$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
---|---|---|---|---|---|
$B%7%s%]%8%&%`(B $B!c%(%s%8%K%"%j%s%0;:6H$N%3%9%H6%AhNO6/2=!d(B | |||||
(9:40$B!A(B10:40)$B!!(B($B:BD9(B $B@nC<7r;J(B) | |||||
O203 | $BBg5,LO%W%i%s%H$N:GE,@_7W(B | plant-wise optimisation catalytic reactor process modelling | S-16 | 1036 | |
O204 | $B%W%m%8%'%/%H$N%j%9%/%^%M!<%8%a%s%H(B | Risk Management Cost | S-16 | 378 | |
O205 | $B2f$,9q$N%(%s%8%K%"%j%s%0;:6H$N6/$_$K$D$$$F(B | Trend Engineering Cost management | S-16 | 65 | |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $B6bC+>;M:(B) | |||||
O206 | $B@_Hw@_7WCJ3,$N(BVE$B3hF0(B | project value enjineering eqipment design | S-16 | 174 | |
O207 | $B%W%i%s%H%3%9%H%G!<%?$N(BPDCA$B%5%$%/%k4IM}$K$D$$$F(B | estimate PDCA Plant cost | S-16 | 455 | |
O208 | $B%W%m%8%'%/%H$NM=B,$K$D$$$F!>(BTCM:Total Cost Management$B$N%U%l!<%`%o!<%/(B | forecast trend variance | S-16 | 1 | |
$B%7%s%]%8%&%`(B $B!c?)IJ9)3X$N:G6a$NE83+$H9b5!G=2=@=IJ$K8~$1$?%"%W%m!<%A!d(B | |||||
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $B:#0f(B $B@5D>(B) | |||||
O213 | [$BE8K>9V1i(B] $BF}2=!&J,;6$H?)$N$*$$$7$5$N4X$o$j(B | Emulsion Dispersion Food | S-28 | 175 | |
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $B | |||||
O215 | $B0!NW3&?eCf$K$*$1$k(B2$B@.J,7O$G$NE|N`$NJ,2rF0NO3X(B | maltose trehalose subcritical water | S-28 | 92 | |
O216 | $B0!NW3&>r7o2<$N%"%;%H%s!&?e:.9g1U$K$h$kC&;iJF9GCj=PJ*$NJ,2h(B | subcritical condition defatted rice bran fractionation | S-28 | 93 | |
O217 | $BD6NW3&Fs;@2=C:AG$K$h$k4;5LN`$N4%Ag2LHi$+$i$N%j%b%M%s$NCj=P>r7o$N:GE,2=(B | limonene supercritical carbon dioxide extraction | S-28 | 805 | |
(14:40$B!A(B15:20)$B!!(B($B:BD9(B $B0BC#(B $B=$Fs(B) | |||||
O218 | $B%j%]%=!<%`FbJq%3%l%9%F%m!<%k$N;@2=H?1~B.EY$K5Z$\$99=@.%j%s;i | kinetic model membrane lipid oxidation | S-28 | 139 | |
O219 | $B5/8;$N0[$J$k%j%Q!<%<$NB?9& | Surface characterization Cross linked immobilization Scanning microscope analysis | S-28 | 476 |