$BD.ED!!MN!JL>8E20Bg3X!K!&;3ED(B $B=(>0!JCO5e4D6-;:6H5;=Q8&5f5!9=!K!&9b66(B $B?-1Q!J?.=#Bg3X!K(B |
$B:G=*99?7F|;~!'(B2021-02-07 15:20:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
CO2 capture | 3$B7o(B | ||
CCUS | 2$B7o(B | ||
piperazine | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
87 | $B5[CeB%?J7?5U%7%U%H%W%m%;%9$K$h$kDc29(BCO$B@=B$(B | CCUS Sorption Enhanced Reaction Reverse Water Gas Shift | O |
139 | CO2$B>:2Z8=>]$rMxMQ$9$k?75,(BCO2$BJ,N%2s<}K!$NDs0F$H4pAC8!F$(B | CO2 Capture Sublimation | O |
193 | [$BE8K>9V1i(B] CO2$BGS=P:o8:$N$?$a$N%+!<%\%s%j%5%$%/%k5;=Q$NJ}8~@-(B | Carbon flow Energy storage Just Transition | O |
232 | $BF<7O6&D@?(G^$N?75,9g@.K!$H$=$N?(G^FC@-(B | CCU Fine Bubble Co-precipitation | O |
244 | [$B0MMj9V1i(B] $BF|4x%0%k!<%W$N(BCCUS$B$KBP$9$k | CCUS | O |
266 | $B%"%_%s(BCO2$B5[<}K!$K$*$1$k:F@8G.M=B,$N$?$a$NG.NO3X%b%G%k$N9=C[(B | CO2 capture Thermodynamic model | O |
477 | 13C-NMR$BJ,8w$K$h$kHs?e7O%"%_%s(BCO2 $B5[<}:^$NG.NO3X8&5f(B | CO2 capture 13C-NMR thermodynamics | O |
490 | $B%T%Z%i%8%s4^M-9bJ,;RKl$K$h$k(BCO2$BJ,N%2s<}(B:$BJ,N%%a%+%K%:%`$N2rL@(B | alkanolamine membrane separation piperazine | O |
848 | $BMM!9$J(BCO2$BJ,05$K$*$$$F(BCO2$B$r2D5U5[<}2DG=$J29EY1~Ez@-%"%_%s4^M-%^%$%/%m%2%kN3;R$N@_7W(B | CO2 separation Chemical absorption pKa | O |
860 | $BC:;@%"%k%+%j5[<}1U$+$i$NM-5!J*$N?eG.9g@.$H5[<}1U:F@8(B | Hydrothermal treatment Formic acid CO2 chemical absorption | O |
861 | $BAjJ,N%7?5[<}1U$rMQ$$$?(BCO2$B5[<}!&:F@8B.EYI>2A5Z$S(BCO2$BJ,N%2s<}AuCV$N@_7W(B | CO2 absorption rate evaluation Device design | O |