$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B |
X$B2q>l(B $BBh(B3$BF|(B |
(9:00$B!A(B12:00) |
9:00$B!A(B 12:00 |
22P001 |
Theoretical modeling of the carbon dioxide absorption by alkanolamines ($BElKLBg1!9)(B) $B!{(B($B3X(B)Ismael Mohamed$B!&(B$B4d(B $B^$B!&(BMart Ugur$B!&(BSahnoun Riadh$B!&(B($B@5(B)$B8E;3(B $BDL5W(B$B!&(B$BDZ0f(B $B=(9T(B$B!&(B($BIt(B)$BH+;3(B $BK>(B$B!&(B($B@5(B)$B1sF#(B $BL@(B$B!&(B($B@5(B)$B9b1)(B $BMN=<(B$B!&(B($BElKLBg1!9)(B/$B2J5;?6$5$-$,$1(B) ($B@5(B)$B5WJ](B $BI4;J(B$B!&(B($BElKLBg1!9)(B) Del Carpio Carlos A.$B!&(B(RITE) $B@6?e(B $B?.5H(B$B!&(B($BElKLBgL$Mh%;%s%?!<(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B | alkabolamine gaseous mixtures theoretical calculations
| S-22 | 738 |
22P002 |
$B%N!<%Q!<%87?(BVPSA$BK!$NC&Ce8=>]$K$D$$$F(B ($B4XEl3X1!Bg(B) $B!{(B($B3X(B)$B8^LZED(B $B9d(B$B!&(B($B@5(B)$BNkLZ(B $B8,0lO:(B$B!&(B($B@5(B)$B9a@n(B $B>[;N(B | PSA
| S-22 | 95 |
22P003 |
VPSA$BK!$K$h$k%H%j%/%m%m%(%A%l%s4^M-GS5$%,%9$NG;=L2s<}(B ($B4XEl3X1!Bg(B) $B!{(B($B3X(B)$BNkLZ(B $B9/9I(B$B!&(B$B@6ED(B $B0lLo(B$B!&(B$B9b;3(B $BNOLi(B$B!&(B($B@5(B)$B9a@n(B $B>[;N(B | PSA
| S-22 | 92 |
22P004 |
Dual Reflux PSA$B%7%_%e%l!<%7%g%s$K$h$k:GE,2=$N8!F$(B ($BL@<#BgM}9)(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B$B!{(B($B3X(B)$B_7ED(B $B7$B!&(B($B3X(B)$B0&9C(B $BCi90(B$B!&(B($B3X(B)$B6b;R(B $B6,(B | Dual PSA simulation
| S-22 | 400 |
22P005 |
$B<~4|E*5[C&CeA`:n$K$*$1$kJ* ($B6bBtBg1!(B) $B!{(B($B3X(B)$BCfB<(B $BBsLi(B$B!&(B($B@5(B)$B;y6L(B $B>$B!&(B($B5[Ce$N8&5f | gas adsorption mass transfer coefficient PSA
| S-22 | 149 |
22P006 |
$B8EE5E}7WNO3X$K4p$E$/%J%N:Y9&FbM"Aw8=>]$N2r@O(B ($BElBg9)(B) $B!{(B($B3X(B)$BFn1@(B $BN<(B$B!&(B($BElKLBg9)(B) ($B@5(B)$B9b1)(B $BMN=<(B$B!&(B($BElBg9)(B) ($B@5(B)$BCfHx(B $B??0l(B | nanoporous material statistical mechanics transport phenomena
| S-22 | 1026 |
22P007 |
FAU$B7?$*$h$S(BMFI$B7?%<%*%i%$%H$X$NM-5!1vAG2=9gJ*$N5[CeB.EY$NB,Dj$HJ,;R%7%_%e%l!<%7%g%s$N8!F$(B ($BL@<#Bg(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B$B!{(B($B3X(B)$B6aF#(B $B??;J(B$B!&(B($B3X(B)$B2CIt(B $B^-0l(B$B!&(B($B3X(B)$B>>K\(B $BN4;V(B | Gravimetric method Micropore diffusivity Molecular Simulation
| S-22 | 534 |
22P008 |
$B=ENLK!$K$h$k:.9gM-5!MO:^>x5$$N%O%$%7%j%+%<%*%i%$%H$K$h$k5[Ce(B ($BL@<#Bg(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B$B!{(B($B3X(B)$B2CIt(B $B^-0l(B$B!&(B($B3X(B)$B6aF#(B $B??;J(B$B!&(B($B3X(B)$B>>K\(B $BN4;V(B | gravimetric method Stop & Go High silica zeolite
| S-22 | 354 |
22P009 |
$BD6NW3&N.BNCf$K$*$1$kM-5!2=9gJ*$N5[Ce%/%m%^%HB,Dj(B ($BL@<#Bg(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B($B3X(B)$BNkLZ(B $BNIB@(B$B!&(B($B3X(B)$B;3:j(B $B7r<#(B$B!&(B$B!{(B($B3X(B)$B0zED(B $BIq0M(B | Supercritical
| S-22 | 412 |
22P010 |
$B%/%m%^%HK!$rMQ$$$?M-5!1vAG2=9gJ*$N%<%*%i%$%H$X$N5[Ce$H!"$=$N5[CeNL0MB8@-(B ($BL@<#Bg(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B$B!{(B($B3X(B)$Bc7F#(B $B7rB@(B$B!&(B($B3X(B)$BCfB<(B $B1Q5*(B$B!&(B($B3X(B)$B6b;R(B $BMN2p(B | chromatograph chlorinated hydrocarbons high silica zeolite
| S-22 | 344 |
22P011 |
$B%/%m%^%HK!$K$h$k(BMSC5A$B$X$NB?@.J,7O%,%95[Ce%7%_%e%l!<%7%g%s(B ($BL@<#BgM}9)(B) ($B@5(B)$B3}86(B $B0lG7(B$B!&(B$B!{(B($B3X(B)$BCfB<(B $B1Q5*(B$B!&(B($B85L@<#BgM}9)(B) ($B3X(B)$B6b;R(B $BMN2p(B | chromatograph stop & go simulation multi component gas
| S-22 | 431 |
22P012 |
$BD>8rG.8r497?5[Ce%V%m%C%/$K$h$kO"B3=|<>A`:n(B ($B6bBtBg1!(B) $B!{4X8}(B $B7<2p(B$B!&(B($B@5(B)$B;y6L(B $B> | dehumidification adsorption heat of adsorption
| S-22 | 153 |
22P013 |
$B5[CeG;=L%W%i%:%^J,2rAuCV$N3+H/(B ($B@>It5;8&(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($B@5(B)$B8ELZ(B $B7$B!&(B($BCfItBg(B) $BB<2,(B $B9n5*(B$B!&(B($B6eBg(B) $B;37A(B $B9,I'(B | Plasma Adsorption Honeycomb
| S-22 | 475 |
22P014 |
$B?e;:2C9)GQ1U$+$iB?9&@-F<(B(II)$B%^%0%M%?%$%H$K$h$k%R%9%A%8%s$H%+%k%N%7%s$N2s<}(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B?5B@O:(B$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 | Adsorption Magnetite Carnosine
| S-22 | 922 |
22P015 |
$B5[CeAj%*%>%s;@2=$K$h$k%H%j%/%m%m%(%A%l%s4^M-?e=hM}$NZ;n83(B ($BElBg@88&(B) $B!{F#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 | ozone adsorption water treatment
| S-22 | 283 |
22P016 |
$B>_L}@=B$9)Dx$+$iGQ4~$5$l$kBgF&Gt$+$i$NM-2A;q8;$NJ,N%%W%m%;%9$N3+H/(B ($B4X@>Bg4D6-ET;T9)(B) $B!{(B($B@5(B)$B;3K\(B $B=($B!&(B($B@5(B)$B7(B<(B $BBg@?(B$B!&(B($B@5(B)$BF#0f(B $BKj;R(B$B!&(B($B@5(B)$B:4!9LZ(B $B:L;R(B | Soy sauce cake Salt flavonoid
| S-22 | 205 |
22P017 |
$B%-%c%C%5%PH/9Z$+$i$NF};@$NJ,N%!&@:@=$K4X$9$k8&5f(B ($BElG@9)Bg(B) $B!{N-(B $B;V1s(B$B!&(B$B2CF#(B $BBYM5(B$B!&(B($B@5(B)$B9q4c(B $B9'M:(B | cassava fermentation azeotropic distillation esterification, hydrolysis
| S-22 | 330 |
22P018 |
$B%$%*%s1UBN$rMQ$$$?@8BNJ,;R$NCj=P%7%9%F%`$N3+H/(B ($B6eBg1!9)(B) $B!{(B($B3X(B)$B>.Lx(B $BM52p(B$B!&(B($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B@5(B)$BCfEg(B $B0l5*(B$B!&(B($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | Ionic Liquids extraction biomolecule
| S-22 | 437 |
22P019 |
$B%9%i%0N.$rMxMQ$7$?>K;@6d?eMO1U$K$h$k(BDHA-Et$BCj=P$K4X$9$kF0NO3XE*8!F$(B ($B2,;3Bg1!4D(B) $B!{(B($B3X(B)$B@62H(B $BM:(B$B!&(B($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B($B@5(B)$B5H_7(B $B=(OB(B$B!&(B($B@5(B)$B>.Ln(B $BEX(B | extraction slug flow DHA
| S-22 | 1067 |
22P020 |
$BD62;GHL82=K!$K$h$k4D6-%[%k%b%s$N=|5n2aDx(B ($BKLBg1!?e(B) $B>>@n(B $BBY9-(B$B!&(B$B!{(B($B@5(B)$B4];3(B $B1QCK(B$B!&(B($B@5(B)$B4X(B $B=(;J(B$B!&(B($B@5(B)$BNkLZ(B $BMc(B | ultrasonic atomization endocrine disruptor chemicals adsorption
| S-22 | 197 |
22P021 |
$BD62;GH6E=8$K$h$k%(%^%k%7%g%sJ,N%$NB%?J(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$B5FK\(B $B=S2p(B$B!&(B($B@5(B)$BFs0f(B $B?8(B$B!&(B($B@5(B)$BFA;3(B $B1Q><(B | ultrasound separation emulsion
| S-22 | 888 |
22P022 |
Preparation of PES hollow fiber membrane and its membrane fouling property ($B?@8MBg1!9)(B) $B!{(B($B3X(B)Rahman Nasrul$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | hollow fiber membrane PES surfactant
| S-22 | 494 |
22P023 |
Effect of membrane preparation condition on PVDF hollow fiber membrane via thermally induced phase separation ($B?@8MBg1!9)(B) $B!{(BRajabzadeh Saeid$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | hollow fiber membrane PVDF thermally induced phase separation
| S-22 | 497 |
22P024 |
$BM[EE;R>CLGK!$K$h$k5U?;F)KlCf$N<+M3BN@QB,Dj$HJ,;R%7%_%e%l!<%7%g%s(B ($B?@8MBg1!9)(B) $BLpGk(B $BAo(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B$B!{(B($B@5(B)$B>>;3(B $B=(?M(B | free volume RO membrane simulation
| S-22 | 506 |
22P025 |
$B%@%$%J%_%C%/8B30_I2a$K$h$k%U%k%\;@!&%U%_%s;@:.9gMO1U$NJ,N%FC@-(B ($BL>Bg9)(B) $B!{(B($B3X(B)$BCfB<(B $BM$;R(B$B!&(B($B@5(B)$B8~0f(B $B9/?M(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | humic substance ultrafiltration rejection
| S-22 | 594 |
22P026 |
$B9ZAG8GDj2=Kl$K$h$k@wNA$NC&?'FC@-(B ($BL>Bg9)(B) $B!{(B($B3X(B)$B>.LZ(B $BM4Fs(B$B!&(B($B@5(B)$BJR6M(B $B@?G7(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | membrane enzyme decolorization
| S-22 | 609 |
22P027 |
$BKlLL79 ($BL>Bg9)(B) $B!{(B($B3X(B)$B9b@P(B $BM-4u;R(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | concentration ultrafiltration optical resolution
| S-22 | 619 |