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$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
monolith | 1$B7o(B | ||
Microreacter | 1$B7o(B | ||
Microreactor | 1$B7o(B | ||
Oscillatory baffled reactor | 1$B7o(B | ||
lithiation reaction | 1$B7o(B | ||
flow | 1$B7o(B | ||
process design | 1$B7o(B | ||
CFD | 1$B7o(B | ||
micro-flow | 1$B7o(B | ||
supercritical carbon dioxide | 1$B7o(B | ||
Hydrosilyration | 1$B7o(B | ||
Sheath flow channel | 1$B7o(B | ||
Micro Space | 1$B7o(B | ||
channel blockage | 1$B7o(B | ||
aldol reaction | 1$B7o(B | ||
Kinetic analysis | 1$B7o(B | ||
Mixing state | 1$B7o(B | ||
Large volume ratio | 1$B7o(B | ||
emulsion | 1$B7o(B | ||
PhotoChlorination | 1$B7o(B | ||
micro flow reactor | 1$B7o(B | ||
Visualization | 1$B7o(B | ||
packed bed reactors | 1$B7o(B | ||
Automation | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
32 | $B9bBN@QHf:.9g8~$1%^%$%/%m%j%"%/%?$N3+H/(B | Microreactor Large volume ratio Sheath flow channel | O |
67 | $B<+F02=%U%m!<<0H?1~AuCV$rMQ$$$?%R%I%m%7%j%k2=H?1~$NB.EYO@E*8!F$(B | Automation Kinetic analysis Hydrosilyration | O |
116 | $B%U%m!2$B%(%^%k%7%g%s$N2D;k2=(B | supercritical carbon dioxide emulsion flow | O |
197 | $B%^%$%/%m%U%m!<%j%A%*2=H?1~$N1?E>0BDj2=5;=Q$N3+H/(B | micro-flow lithiation reaction channel blockage | O |
335 | $B%^%$%/%m%9%1!<%k$N?6F0N.%P%C%U%kH?1~4o$NFbItN.F04Q;!(B | Oscillatory baffled reactor Mixing state Visualization | O |
562 | $B?(G^8GDj2=B?9& | micro flow reactor aldol reaction monolith | O |
612 | $B= | packed bed reactors CFD process design | O |
747 | $B%^%$%/%m6u4V$rMQ$$$?8w1vAG2=H?1~$N8!F$(B | PhotoChlorination Micro Space Microreacter | O |