$BBh(B1$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
$BJ,N%%W%m%;%9(B |
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $B>.?{!!?M;|(B) |
9:40$B!A(B 10:00 | F103 | $BB?@.J,7O%$%*%s8r49$K$*$1$k%+%i%`$X$NL$:F@8 ($B2#9qBg9)(B) $B!{(B($B3X(B)$B;V2l(B $BM42p(B$B!&(B($B@5(B)$BCfB<(B $B0lJf(B$B!&(B($B@5(B)$B?7ED8+(B $B6)(B$B!&(B($B@5(B)$B>>K\(B $B44<#(B | ionexchange breakthrough curve model
| 4-e | 763 |
10:00$B!A(B 10:20 | F104 | $B9bI=LL@Q%^%0%M%?%$%H$ND4@=$HbgAG=|5nFC@-$NI>2A(B ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBg\F(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | adsorption magnetite arsenic
| 4-e | 65 |
10:20$B!A(B 10:40 | F105 | $BCj=P:^FbJq%^%$%/%m%+%W%;%k$K$h$k(BNi$B!"(BCo$B$NJ,N%(B ($BF1;V$B!&(B($B@5(B)$B>>K\(B $BF;L@(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B | metal adsorption microcapsule
| 4-e | 69 |
10:40$B!A(B 11:00 | F106 | Ft-ir$B$rMQ$$$?B?9&2A$H%$%*%s5[Ce7ABV$N8!F$(B ($B5~Bg1!9)(B) $B!{(B($B@5(B)$BKR(B $BBYJe(B$B!&(B($B3X(B)$BKY8}(B $B>4B@(B$B!&(B($B@5(B)$BA0(B $B0lW"(B | FeOOH phosphoric ion sulfate ion
| 4-e | 210 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BKR!!BYJe(B) |
11:00$B!A(B 11:20 | F107 | $B%/%(%s;@$r:x2==u:^$H$7$?B?9& ($B | divalent metal porous glass separation
| 4-e | 250 |
11:20$B!A(B 11:40 | F108 | Adsorption of Metal Ions by Composite Chitosan Beads ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)Doldina Meruyert$B!&(B($B@5(B)$B>.?{(B $B?M;|(B | Adsorption Chitosann composite Metal ion
| 4-e | 593 |
11:40$B!A(B 12:00 | F109 | $B%^%0%M%?%$%H$*$h$S%^%0%M%?%$%H(B-$B%-%H%5%sHyN3;R$ND4@=$H(BAs($B-7(B)$B$H(BAs($B-9(B)$B$N5[CeJ?9U(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$BF|9b(B $BM&2p(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | arsenic magnetite chitosan
| 4-e | 635 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B5WJ]ED(B $BIY@8;R(B) |
13:00$B!A(B 13:20 | F113 | $BA+0\6bB0C4;}%-%l!<%H ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B$BN);3(B $BJfDEH~(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | Immobilized metal affinity adsorption carnosine
| 4-e | 162 |
13:20$B!A(B 13:40 | F114 | $B%0%i%U%H2=%-%H%5%sM6F3BN$ND4@=$H5.6bB05[CeFC@-$NI>2A(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B9uLZ(B $BM5B@(B$B!&(B($B%a%k%\%k%sBg(B) Stevens Geoff. W.$B!&(BM. Perera Jilska$B!&(BD. Kolev Spas$B!&(B($B5\:jBg9)(B) ($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | adsorption chitosan precious metal
| 4-e | 753 |
13:40$B!A(B 14:00 | F115 | 2-$B%"%_%N%a%A%k%T%j%8%s4^?/ ($BET>k9b@l(B) $B!{(B($B3X(B)$BFn(B $BBs(B$B!&(B($B@5(B)$B4d7'(B $BH~F`;R(B$B!&(B($B5\:jBg(B) ($B@5(B)$BGO>l(B $BM3@.(B | impregnated resin palladium
| 4-e | 331 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BBgEg!!C#Li(B) |
14:00$B!A(B 14:20 | F116 | $B??6u%]%s%WL}$K$h$k6b$NMOG^Cj=P(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B0$It(B $BL-(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B | Vacuum pump oil gold solvent extraction
| 4-e | 325 |
14:20$B!A(B 14:40 | F117 | $B?75,%j%0%K%s%2%k$N3+H/$*$h$S5.6bB0$N2s<}(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B>>;^(B $BH~9,(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B$B!&(B($B;0=EBg@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B | wheat lignophenol precious metal
| 4-e | 260 |
14:40$B!A(B 15:00 | F118 | $B%J%H%j%&%`1v7?%_%+%s%8%e!<%9%+%95[Ce:^$N6bB0%$%*%s5[CeFC@-(B ($B:42lBgM}9)(B) $B!{:M86(B $B9'0l(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B3X(B)$B0f>e(B $B=a0l(B | Adsorption Orange waste Heavy metals
| 4-e | 717 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BBg\F!!70(B) |
15:00$B!A(B 15:20 | F119 | $B%_%+%s%8%e!<%9%+%9$rMQ$$$?6b$N5[Ce!&2s<}(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B0$It(B $BL-(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B | polyphenol gold adsorption orange juice residue
| 4-e | 328 |
15:20$B!A(B 15:40 | F120 | PEG$B%O%$%I%m%2%k$X$N5.6bB0N`$N5[Ce(B ($BL>Bg9)(B) $B!{(B($B3X(B)$B0KF#(B $B>00o(B$B!&(B($B@5(B)$BFs0f(B $B?8(B$B!&(B($BL>8E20;T9)8&(B) ($B@5(B)$BLZ2<(B $BIpI'(B$B!&(B$B@P3@(B $BM';0(B$B!&(B$BCfLn(B $BK|7I(B$B!&(B$B;38}(B $B9@0l(B$B!&(B$B=)ED(B $B=E?M(B | hydrogel poly(ethylene glycol) precious metal
| 4-e | 461 |
15:40$B!A(B 16:00 | F121 | $B%"%k%+%j=hM}$r;\$7$?@=;f%9%i%C%8>F5Q3%$NFC@-$H$=$N1~MQ(B ($B=)EDBg9);q(B) $B!{(B($B@5(B)$BOBEh(B $BN4>;(B | paper sludge ash alkali activation water purification
| 4-e | 16 |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $BFs0f!!?8(B) |
16:00$B!A(B 16:20 | F122 | $B%$%*%s8r49IT?%I[%Y%k%H<0J,N%AuCV$K$h$k%j%s;@$HM-5!;@$NO"B3J,N%(B ($B:eI\Bg1!9)(B) $B!{(B($B3X(B)$B1J86(B $B=(98(B$B!&(B($B@5(B)$B5HED(B $B90G7(B$B!&(B($B@5(B)$BCfB<(B $B=(H~(B | separation ion-exchange adsorption
| 4-e | 409 |
16:20$B!A(B 16:40 | F123 | ($B7gHV(B)
|
| 100 | 230 |
$BBh(B2$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
$BJ,N%%W%m%;%9(B |
(9:20$B!A(B10:20)$B!!(B($B:BD9(B $BDT!!CRLi(B) |
9:20$B!A(B 9:40 | F202 | $B%P%$%*%(%?%N!<%k$NH/9Z1U$+$i$N1UAj5[Ce$K$h$kG;=L!&2s<}(B ($BElBg@88&(B) $B!{(B($B3X(B)$B$B!&(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | bioethanol adsorption recovery
| 4-e | 139 |
9:40$B!A(B 10:00 | F203 | $B%P%$%*%(%?%N!<%kCf$NN22+7OIT=cJ*=|5n$rL\E*$H$7$?6bB0C4;}B?9& ($B;:Am8&(B) $B!{(B($B@5(B)$B;3K\(B $BBs;J(B$B!&(B($B@5(B)Chaichanawong Jintawat$B!&(B($B@5(B)$BBg?9(B $BN4IW(B | liquid phase adsorption porous carbon dimethylsulfide
| 4-e | 193 |
10:00$B!A(B 10:20 | F204 | IMAC$BK!$H8B30$m2a$rAH$_9g$o$;$?%R%9%A%8%s4^M-%Z%W%A%IJ,N%K!$N3+H/(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B7s;0(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | ultrafiltration carnosine metal affinity
| 4-e | 750 |
(10:20$B!A(B11:20)$B!!(B($B:BD9(B $BM>8l!!9nB'(B) |
10:20$B!A(B 10:40 | F205 | $B5[CeG.$K$h$k29EY>e>:$NM^@)$rL\E*$H$7$?C_G.5!G=$rM-$9$k5[Ce:^$N3+H/(B ($BElBg@88&(B) $B!{(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | phase change material carbon dioxide adsorption heat
| 4-e | 365 |
10:40$B!A(B 11:00 | F206 | $BDc29:F@8%G%7%+%s%H%m!<%?$N@EE*$*$h$SF0E*5[CeFC@-8&5f(B ($B@>It5;8&(B) $B!{(B($B@5(B)$B6b(B $B0NNO(B$B!&(B($B@5(B)$B2,Ln(B $B9@;V(B$B!&(B($B@5(B)$B0f>e(B $B9(;V(B$B!&(B($B5[Ce$N8&5f | Desiccant rotor Adsorption Dehumidifier
| 4-e | 724 |
11:00$B!A(B 11:20 | F207 | $B?eAG5$N.Cf$K$*$1$k%H%k%(%s(B+$B%a%A%k%7%/%m%X%-%5%s$N3h@-C:$X$N5[CeFC@-$HG3NAEECS?eAGCyB"G^BN$X$N1~MQ(B ($BF|Bg@8;:9)(B) $B!{(B($B3X(B)$BCfN$(B $BM'B'(B$B!&(B($B@5(B)$BDT(B $BCRLi(B$B!&(B($B@5(B)$BF|=)(B $B=SI'(B$B!&(B($B1'ET5\Bg9)(B) ($B@5(B)$B0KF#(B $BD> | Fuel Cell Hydrogen Adsorption
| 4-e | 70 |
(11:20$B!A(B12:00)$B!!(B($B:BD9(B $B;3K\!!Bs;J(B) |
11:20$B!A(B 11:40 | F208 | $BAjJQ2=J* ($BElBg@88&(B) $B!{(B($B3X(B)$BB<>e(B $BM:B@(B$B!&(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | PSA PCM adsorption
| 4-e | 295 |
11:40$B!A(B 12:00 | F209 | $B>J%(%M%k%.!<7?05NO%9%$%s%05[CeK!$K$h$k?75,(BCO2$BJ,N%2s<}5;=Q$N3+H/(B (RITE) $B!{(B($B@5(B)$B5\K\(B $B3X(B$B!&(B($BF`NI@hC$B!&(B(RITE,$BF`NI@hC8l(B $B9nB'(B$B!&(B(RITE) $BF#2,(B $BM40l(B | carbon dioxide capture and separation adsorption
| 4-e | 347 |
$BBh(B3$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
$BJ,N%%W%m%;%9(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B2<>r!!98;JO:(B) |
9:00$B!A(B 9:20 | F301 | $B5U%_%;%k$rMQ$$$?0lK\:?3K;@Cj=P$K$*$1$k(BDNA$B3&LL3h@-:^$N1F6A(B ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@PDE(B $BD>$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B6eBg1!9)(B) $B:YLZ(B $BBnLi(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | DNA micelle extract
| 4-f | 683 |
9:20$B!A(B 9:40 | F302 | $B%/%i%&%s%(!<%F%k$H$N:x7A@.$rMxMQ$7$??e@-FsAj7O$K$*$1$k%?%s%Q%/ ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B$BKv$B!&(B($B3X(B)$B9CHe(B $B@i2F(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | aqueous two-phase system crown ether protein
| 4-f | 166 |
9:40$B!A(B 10:00 | F303 | W/O/W$B%(%^%k%7%g%sK!$K$h$kL55!Cf6uHyN3;R$ND4@=(B ($BBgJ,Bg9)(B) $B!{(B($B3X(B)$B;05\(B $B?5Li(B$B!&(B($B@5(B)$BT"J,(B $B=$;0(B$B!&(B($B@5(B)$BDL:e(B $B1I0l(B$B!&(B($B@5(B)$BJ?ED(B $B@?(B | microballoon emulsion interfacial reaction
| 4-f | 159 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>>K\!!F;L@(B) |
10:00$B!A(B 10:20 | F304 | $B%W%m%j%s%"%k%-%kM6F3BN$N9g@.$H%l%"%a%?%kJ,N%!&2s<}$X$N1~MQ(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B?5B@O:(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | rare metal separation extraction
| 4-f | 627 |
10:20$B!A(B 10:40 | F305 | $B8~N.@\?(%9%W%l! ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BA}ED(B $BIRLi(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | spray column coal tar absorption oil extraction rate
| 4-f | 450 |
10:40$B!A(B 11:00 | F306 | $B%$%*%s1UBN;Y;}1UKl$K$*$1$k%3!<%k%?!<%k5[<}L}$NF)2a(B ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BEgED(B $B5AG7(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | ionic liquid supported liquid membrane coal tar absorption oil
| 4-f | 446 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B9>F,!!N50l(B) |
11:00$B!A(B 11:20 | F307 | $B%8%"%_%I7OG[0L;R$rMQ$$$?%$%*%s1UBNCj=P7O$N9=C[(B ($B86;RNO5!9=(B) $B!{(B($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B$BAR66(B $B7r2p(B$B!&(B($B@5(B)$BD9Fl(B $B90?F(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids solvent extraction separation
| 4-f | 119 |
11:20$B!A(B 11:40 | F308 | $B%+%k%\%s;@7O?75,Cj=P:^$K$h$k4uEZN`6bB0$N%$%*%s1UBNCj=P(B ($B6eBg1!9)(B) $B!{(B($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B3X(B)$B>.Lx(B $BM52p(B$B!&(B($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$BCfEg(B $B0l5*(B$B!&(B($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids rare earth extraction
| 4-f | 443 |
11:40$B!A(B 12:00 | F309 | $BF};@J,N%$X$N%$%*%s1UBN4^?;Cf6u;eKl$N1~MQ(B ($BF1;V$B!&(B($B@5(B)$B>>K\(B $BF;L@(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B$B!&(B($BK-EDCf8&(B) ($B@5(B)$BEhB<(B $BN4(B$B!&(B($B@5(B)$BDT(B $B@5CK(B | Liquid membrane Lactic acid Hollow fiber
| 4-f | 178 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B>>ED!!7=8g(B) |
13:00$B!A(B 13:20 | F313 | $B%P%$%*%(%?%N!<%kG;=L%W%m%;%9$N(BHIDiC$B2=$N8!F$(B ($B4X@>2=3X(B) $B!{(B($B@5(B)$BJR2,(B $BK.IW(B$B!&(B($B@5(B)$BLnED(B $B=(IW(B$B!&(B($B@5(B)$B;3O)(B $B42;J(B$B!&(B($B@5(B)$BARC+(B $B?-9T(B$B!&(B($B@5(B)$B6bED(B $BK|J?(B$B!&(B($B@5(B)$B8~ED(B $BCi90(B | Energy-saving Distillation Bioethanol Production HIDiC
| 4-c | 17 |
13:20$B!A(B 13:40 | F314 | $BH/9Z1UM3Mh(BL-$BF};@$N%(%9%F%k2=!"2C?eJ,2r$K$h$k@:@=(B ($BElG@9)Bg9)(B) $B!{(B($B@5(B)$BK\B?(B $BB@$B!&(B($B@5(B)$B9q4c(B $B9'M:(B$B!&(B$B2CF#(B $BBYM5(B | lactic acid reactive distillation fermentation broth
| 4-c | 755 |
13:40$B!A(B 14:00 | F315 | Application of a Fully Thermally Coupled Distillation Column for Practical Azeotropic Separation (Dong-A U.) Sung Ick Gi$B!&(B$B!{(B($B@5(B)Kim Young Han | Energy-Efficient Distillation Thermally Coupled Distillation Azeotropic Distillation
| 4-c | 26 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;3K\!!=( |
14:00$B!A(B 14:20 | F316 | $B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= ($B>xN1MQ5,B'= | Linear Flow High Liquid Hold High Operating Capacity
| 4-c | 39 |
14:20$B!A(B 14:40 | F317 | $BC1>xN1 ($BF|BgM}9)(B) $B!{(B($B3X(B)$BK\66(B $B8-E5(B$B!&(B($B%*%a%,%7%_%e%l!<%7%g%s(B) ($B@5(B)$B2#;3(B $B9n8J(B$B!&(B($BF|BgM}9)(B) ($B@5(B)$B>>ED(B $B909,(B$B!&(B($B@5(B)$B7*86(B $B@6J8(B$B!&(B($B@5(B)$BFJLZ(B $B>!8J(B | Simple Distillation Estimation of Components Change of Temperature
| 4-c | 217 |
14:40$B!A(B 15:00 | F318 | TAME$B9g@.H?1~>xN1%W%m%;%9$NHsDj>o%7%_%e%l!<%7%g%s(B ($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B0f9x(B $BC#O:(B$B!&(B($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B | reactive distillation dynamic simulation TAME
| 4-c | 324 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BFJLZ!!>!8J(B) |
15:00$B!A(B 15:20 | F319 | $B= ($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | flooding packed column distillation
| 4-c | 613 |
15:20$B!A(B 15:40 | F320 | $B= ($BLZB<2=9)5!(B) $B!{@>ED(B $B<~9T(B$B!&(B($B@5(B)$BCf@>(B $B=S@.(B$B!&(B$BB-N)(B $B>0fb(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B | HIDiC Distillation proccess design
| 4-c | 761 |
15:40$B!A(B 16:00 | F321 | $B5$1UJ?9U$K5Z$\$91v8z2L$rMxMQ$7$?:.9gGQ;@$+$i$N;@$N>xN1J,N%(B ($B4X@>Bg4D6-ET;T9)(B) ($B@5(B)$B;3K\(B $B=($B!&(B$B!{(B($B3X(B)$BIMED(B $BM5;0(B$B!&(B($B3X(B)$BJ?Ln(B $B@5?M(B$B!&(B$BD.Ln(B $B>-9((B$B!&(B($B?9ED2=3X9)6H(B) $BI4ED(B $BK.t!(B | waste acid distillation recycle
| 4-j | 597 |