| $B>>K\(B $B=(9T!JEl5~9)6HBg3X!K!&>>ED(B $B7=8g!J;37ABg3X!K!&J!Eg(B $B9/M5!JElKLBg3X!K(B |
$B3W?7E*%W%m%;%95;=Q$NAO@.$rL\;X$9%W%m%;%96/2=8&5f$O!";}B32DG= $B"(K\%;%C%7%g%s$O(BSIS$BIt2q>^$N?3::BP>]$H$J$j$^$9!#(B
$B:G=*99?7F|;~!'(B2022-01-31 16:50:01
 $B$3$NJ,N`$G$h$/;H$o$l(B$B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| Membrane | 2$B7o(B |  | |
| Mass Transfer | 2$B7o(B | | |
| CFD | 2$B7o(B | | |
| Separation | 2$B7o(B | | |
| machine learning | 2$B7o(B | | |
| economic and environmental indicators | 1$B7o(B | | |
| $B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $BH/I=7A<0(B | |
|---|---|---|---|
| 47 | $B>xN1%W%m%;%9$NJ?9U7O%b%G%k$+$i8= | Packed Column Distillation Mass Transfer Model Concept | O |
| 49 | 3$B@.J,M}A[7O$N= | Mass Transfer Packed Distillation Column Two Film Theory | O |
| 83 | $B5!3#3X=,$rMQ$$$?%O%$%V%j%C%I(BPFR$B%b%G%k(B | Plug-flow reactor Machine learning Ammonia synthesis | O |
| 152 | CO2$BJ,N%$rBP>]$H$7$?%"%_%s5[<}(B-$BKl%O%$%V%j%C%I%W%m%;%9$N%F%/%N%(%3%N%_%C%/2r@O(B | Separation Membrane Carbon dioxide | O |
| 165 | $BJ,;67?%(%M%k%.!<6!5k$N$?$a$NHs6&J(:.9gG^BN$rMQ$$$?>.7?%P%$%J%j! | Renewable energy distributed energy system micro ORC | O |
| 251 | PEFC$BMQ?(G^%9%i%j!<$N:.9gD4@=%W%m%;%92r@O$K$*$1$k%l%*%m%8!<%G!<%?E,MQJ}K!$N8!F$(B | data analysis rheology polymer electrolyte fuel cell | O |
| 254 | Pt/TiO2$B?(G^$rMQ$$$?(BNO$B$+$i(BNH3$B$X$NJQ49H?1~$K$*$1$k6!5kG;EYJQF0A`:n$N1F6A(B | unsteady-state operation NOx to Ammonia nitrogen cycle | O |
| 310 | $B9bG4@-N.BN$X$N1~MQ$rL\;X$7$??6F0N.%P%C%U%kH?1~4oFb$NN.F02r@O$H:.9g>uBV$NI>2A(B | Oscillatory Baffled Reactor mixing CFD | O |
| 336 | FO$BKl$rMQ$$$?4uGv1v2=%"%s%b%K%&%`?eMO1UJ,N%%W%m%;%9$N@_7W(B | Separation Membrane Forward osmosis | O |
| 437 | $B?6F0J?HD>e$K@_CV$7$?1UE)Fb$N:.9g$K5Z$\$9=[4DN.F0$N8z2L(B | Microfluid Droplet Reactor CFD | O |
| 511 | $B%J%N%U%!%$%P!<$rMQ$$$?<+8J=$I|@-KI?)%3!<%F%#%s%0$K$*$1$k=$I|:^$NJ|=P%7%_%e%l!<%7%g%s(B | Self-healing Cellulose nanofiber Molecular-dynamics simulation | O |
| 593 | $B29EYJ,I[$rM-$9$k%F%$%i!<12N.$N%@%$%J%_%/%9$KN.BNJ*@-$,5Z$\$91F6A(B | Taylor vortex flow Thermal convection Heat/mass transfer | O |
| 641 | $BJ,;R>pJs$rF~NO$7$?5!3#3X=,$K$h$kAjJ,N%7?(BCO2$B5[<}:^$NAj5sF02r@O(B | CO2 capture phase separation absorbent machine learning | O |
| 697 | $B%@%$%J%_%C%/$KJQMF$9$k30ItMW0x$N$b$H$G$ND6DcC:AG2=2=3X%W%m%;%9$N@_7W$X$N2]Bj(B | carbon neutral process design | O |
| 736 | Assessment of Potential Use of Rice Husk for Tetraethyl Orthosilicate Production | Tetraethyl orthosilicate rice husk economic and environmental indicators | O |
| 773 | Assessing the environmental impact of catalyst selectivity patterns on waste plastic reforming | Plastic waste reforming Plastic LCA Environmental impact assessment | O |
| 776 | $B@8BNJ,;R$NA*BrE*5[Ce%W%m%;%9$r@_7W$9$k$?$a$N%^%F%j%"%k%:!&%$%s%U%)%^%F%#%/%95;=Q(B | Materials informatics Biomolecule Selective absorption | O |
| 832 | $BO"B3<0?6F0N.%P%C%U%kH?1~4o$K$h$k>=@O%W%m%;%9$N6/2=(B | Continuous crystallization Chaotic mixing Process Intensification | O |
| 861 | $B3IYB$K$h$j3&LLJ* | Distillation Continuous operation HETP | O |
| 866 | $B?75,(BCO2$BMxMQ2=3XIJ9g@.%W%m%;%93+H/;X?KDs0F | CCU LCA Process simulation | O |
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B52$B2s=)5(Bg2q(B ($B2,;3(B)
(C) 2022 $B8x1WMost recent update: 2022-01-31 16:50:01
For more information contact $B2=3X9)3X2q(B $BBh(B52$B2s=)5(Bg2q(B $B
E-mail: inquiry-52f
www3.scej.orgThis page was generated by 
easp 2.46; update.pl 2.37 (C)1999-2015 kawase
easp 2.46; update.pl 2.37 (C)1999-2015 kawase