$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B $B!cCj=P!&%$%*%s8r49!&5[Ce!!!A4pAC$H1~MQ!A!d(B | |||||
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B;y6L(B $B> | |||||
R104 | $BD6NW3&(BCO2$BCf$K$*$1$k3h@-C:$X$N(BVOC$B5[Ce$NB.EYO@E*2r@O(B | Supercritical carbon dioxide Adsorption kinetics Activated carbon | S-20 | 157 | |
R105 | $BDLEE2CG.%"%k%^%$%HG3>F?(G^$H5[CeG;=L9)Dx$+$i$J$k%O%$%V%j%C%I(BVOCs$B=hM}%7%9%F%`$N8&5f!<(B2$B@.J,7O%,%9$G$N5[C&Ce;n83$H5[C&Ce%7%9%F%`$N8!F$!<(B | VOC adsorption activated carbon | S-20 | 519 | |
R106 | $B%U%'%N!<%k7O | Activated carbon adsorption | S-20 | 423 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BNS(B $B=g0l(B) | |||||
R107 | $B0lJ}8~E`7k$rMQ$$$?%U%'%N!<%k$+$i$N%^%$%/%m%O%K%+%`>u%+!<%\%s$N:n@=$HFC@-I>2A(B | Carbon Microhoneycomb Unidirectional freezing Sol-gel polycondensation | S-20 | 142 | |
R108 | $B?e>x5$$r4^$`Fs@.J,:.9g%,%9J?9U5[CeNL$NB,Dj$H2r@O(B | equilibrium adsorption capacity VOC water vapor | S-20 | 234 | |
R109 | $BL55!7O5[Ce:`%O%9%/%l%$$N(BNMP$B5[Ce@-G=I>2A(B | HAS-Clay N-methylpyrrolidinone adsorption | S-20 | 381 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BBgEO(B $B7<2p(B) | |||||
R113 | [$BM%=(O@J8>^(B]Application of Ionic Liquids to Extraction Separation of Rare Earth Metals with an Effective Diglycol Amic Acid Extractant | Extraction Ionic liquid rare earth | S-20 | 42 | |
R115 | $B%l%"%a%?%k$NO"B38~N.K"KwJ,N%$G$NEc7B3HBg$K$h$kJ,N%$N8~>e(B | Foam Separation Gold Gallium | S-20 | 723 | |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B$O$P$-(B $B9-82(B) | |||||
R116 | $B%8%A%*%+!<%P%a!<%H7?Cj=P:^$rMQ$$$?0!1t$+$i$N%+%I%_%&%`$NA*BrE*Cj=P(B | extraction trident-molecules cadmium | S-20 | 804 | |
R117 | $BJ#AG4D7?;05S>uJ,;R$rMQ$$$?5.6bB0$NCj=P!&J,N%(B | extraction trident molecule precious metals | S-20 | 805 | |
R118 | $BCj=P:^4^?;%+%]%C%/%U%!%$%P!<$K$h$k4uEZN`6bB0$N5[CeJ,N%(B | solvent impregnated fiber separation rare earth metals | S-20 | 61 | |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B@>IM(B $B>OJ?(B) | |||||
R119 | $B%"%k%-%k:?$rF3F~$7$?AB?e2=4^CbAGB?:BG[0L;R$K$h$k=E6bB0J,N%(B | solvent extraction metal separation multidentate ligand | S-20 | 896 | |
R120 | $B%b%s%4%k;:E7A3%<%*%i%$%H$K$h$kB?@.J,=E6bB0$r4^$`9[;3GQ?e$N5[Ce(B | Mongolian natural zeolite mine wastewater heavy metal | S-20 | 486 | |
R121 | $B;0 | Electrochemically switched ion exchange Cesium separation Nickel hexacyanoferrate | S-20 | 109 | |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $BFs0f(B $B?8(B) | |||||
R122 | $BF}2=1UKl$K$h$k@PL}7OJ,2rEtL}$+$i$NK'9aB2J,N%(B | cracked kerosene aromatic recovery emulsion liquid membrane | S-20 | 782 | |
R123 | $B:.9gMOG^$rMQ$$$?1U1UCj=P$K$h$k%P%$%*%(%?%N!<%k$NG;=L(B | Bioethanol concentration Mixed solvent Liquid-liquid extraction | S-20 | 869 | |
R124 | $B?e@-FsAjK!$K$h$k(B2,3-$B%V%?%s%8%*!<%k$NCj=PJ,N%(B | Extraction Aqueous two phase butanediol | S-20 | 162 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B $B!cJ,N%%W%m%;%9It2q%7%s%]%8%&%`!d(B | |||||
(9:00$B!A(B10:20)$B!!(B($B:BD9(B $BFn1@(B $BN<(B) | |||||
R201 | PSA$BK!$K$h$k9bO'%,%9$+$i$N(BCO2$BJ,N%5;=Q$N3+H/(B | pressure swing adsorption blast furnace exhaust gas CO2 separation | S-22 | 52 | |
R202 | CeO2$B7OJ#9g;@2=J*I=LL$K$*$1$k(BCO2$B5[Ce9=B$(B | CO2 adsorption CeO2 | S-22 | 173 | |
R203 | RHO$B7?%<%*%i%$%H$rMQ$$$?Fs;@2=C:AGJ,N%:`NA$N3+H/(B | Zeolite rho Carbon dioxide Ion-exchange | S-22 | 751 | |
R204 | $B%V%?%sMO:^$rMQ$$$?%P%$%*%(%?%N!<%kG;=LC&?e>J%(%M%k%.!<2=(B | bioethanol n-butane dehydration | S-22 | 287 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BD.ED(B $BMN(B) | |||||
R213 | $B7rA4$J5$1UJ?9U%G!<%?$rMQ$$$k(B3$B@.J,7O%l%7%8%e%"%k6J@~$H>xN17W;;(B | Residual curve Distillation calculation Consistent VLE data | S-22 | 399 | |
R214 | $B2~NI7?(BPetlyuk$B>xN1%W%m%;%9$N>J%(%M%k%.! | modified Petlyuk process simulation energy saving | S-22 | 425 | |
R215 | $B2~NI7?(BPetlyuk$B>xN1$N>J%(%M%k%.!<@-8!F$(B | Distillation Petlyuk Energy Conservation | S-22 | 599 | |
(14:00$B!A(B15:20)$B!!(B($B:BD9(B $B@V>>(B $B7{ | |||||
R216 | ($B9V1iCf;_(B) | 100 | 601 | ||
R217 | $BJ,N%%W%m%;%9$K$*$$$F05NO$NJQ2=$r9MN8$7$F6&J(M=B,$r9T$&E}7W%b%G%k$N9=C[(B | azeotrope SVM pressure | S-22 | 602 | |
R218 | $B>xN1(B/$BKlJ#9g%W%m%;%9$N9=@.$HJ,N%FC@-(B | Hybrid distillation process Membrane separation Vapor permeation | S-22 | 738 | |
R219 | Intensification of heat integrated distillation columns (HIDiCs) through external heat integration | Optimization HIDiC distillation Process Intensification | S-22 | 837 |