$BKY9>(B $B9';K!JBg:e8xN)Bg3X!K!&JR2,!!{D!J;:6H5;=QAm9g8&5f=j!K!&>>K\(B $B=(9T!JEl5~9)6HBg3X!K(B |
SDGs$B$NC#@.$dCO5e$N8B3&$r2r7h$9$k$?$a$K!$
$B:G=*99?7F|;~!'(B2023-05-14 05:35:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
Ammonia | 1$B7o(B | ||
catalyst slurry | 1$B7o(B | ||
Cultivation | 1$B7o(B | ||
Laminar mixing | 1$B7o(B | ||
mixing | 1$B7o(B | ||
MOF | 1$B7o(B | ||
Ru catalyst | 1$B7o(B | ||
Polyvinyl formal resin | 1$B7o(B | ||
time variation | 1$B7o(B | ||
Feed factor | 1$B7o(B | ||
Therapeutec Protein | 1$B7o(B | ||
Unutilized biomass | 1$B7o(B | ||
Multi-Production | 1$B7o(B | ||
Ion exchange resin method | 1$B7o(B | ||
Ammonia synthesis | 1$B7o(B | ||
Ruthenium | 1$B7o(B | ||
Green ammonia | 1$B7o(B | ||
H2/N2 ratio | 1$B7o(B | ||
Dynamic simulation | 1$B7o(B | ||
CFD | 1$B7o(B | ||
Membrane separation | 1$B7o(B | ||
Immobilization | 1$B7o(B | ||
Multi-component powder | 1$B7o(B | ||
process intensification | 1$B7o(B | ||
process simulation | 1$B7o(B | ||
Reaction pathway | 1$B7o(B | ||
optimization | 1$B7o(B | ||
separation | 1$B7o(B | ||
PSA | 1$B7o(B | ||
Renewable hydrogen | 1$B7o(B | ||
ultrasound | 1$B7o(B | ||
distillation column | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
123 | [$B0MMj9V1i(B] $B86NA%,%9$rJ,3d6!5k$9$k$3$H$K$h$j@8;:G=$r9b$a$?(BNH3$B9g@.AuCV$N3+H/(B | Ammonia synthesis Ru catalyst H2/N2 ratio | O |
175 | $B%@%$%J%_%C%/%7%_%e%l!<%7%g%s$rMQ$$$?:`NAFC@-I>2A$H%W%m%;%9$N8!F$$K$h$k(BCO2$B5[CeJ,N%%7%9%F%`$N@_7W(B | PSA CO2 separation | O |
180 | $B%"%s%b%K%"9g@.MQ(BRu/CeLaOx$B?(G^$X$N(BSi$BE:2C8z2L(B | Ammonia Ruthenium | O |
304 | Pt/C$B?(G^%9%i%j!<$N:.9gA`:n;~4V$,8G1UJ,;65sF0$K5Z$\$91F6A$N2r@O(B | mixing time variation catalyst slurry | O |
332 | $B%W%m%T%l%sJ,N%$K$*$1$k%3%9%H$H(BCO2$BGS=PNL$r9MN8$7$?(B2$BCJKlJ,N%%7%9%F%`$N@_7W(B | Membrane separation Total annual cost CO2 emission | O |
355 | $BO"B3@:N1Ec%W%m%;%9%7%_%e%l!<%7%g%s<+F0:GE,2=%7%9%F%`$N3+H/(B | process simulation distillation column optimization | O |
383 | $BB?9&@-N3;R$rMQ$$$?Hy:YAtN`$N8GDj2=%W%m%;%9(B | Microalgae Immobilization Polyvinyl formal resin | O |
517 | $B%D%$%s%9%/%j%e!<%U%#!<%@$G$N(B2$B@.J,:.9gKv%U%#!<%I%U%!%/%?! | Process modeling Feed factor Multi-component powder | O |
577 | $B86Lt9g@.$K$*$1$kK'9aB25a3KCV49H?1~$NB.EYO@E*%b%G%j%s%0(B | Nucleophilic aromatic substitution Kinetic study Reaction pathway | O |
589 | $B%@%$%J%_%C%/%7%_%e%l!<%7%g%s$H5$>]%G!<%?$r3hMQ$7$?%0%j!<%s%"%s%b%K%"@=B$%W%m%;%9$N@_7W(B | Renewable hydrogen Green ammonia Dynamic simulation | O |
645 | $B%b%N%/%m!<%J%k93BN@=B$%W%m%;%9$N%7%_%e%l!<%7%g%s$H@_7W$X$N1~MQ(B | Chromatography Cultivation Therapeutec Protein | O |
721 | $B?6F0N.%P%C%U%kH?1~4oFb$N(BCFD$BN.F02r@O$K$h$kAXN.:.9g$NI>2A(B | Oscillatory flow Laminar mixing CFD | O |
726 | $B6bB0M-5!9=B$BNHyN3;R9g@.%W%m%;%9$K5Z$\$9D62;GH>H | ultrasound MOF process intensification | O |
843 | [$B>7BT9V1i(B] $B7P:QE*$J;q8;=[4D$r | Unutilized biomass Multi-Production Ion exchange resin method | O |