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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 |
(C) 2021 $B8x1W
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