
$B:G=*99?7F|;~!'(B2017-10-04 20:22:01
$B$3$NJ,N`$G$h$/;H$o$l(B$B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| membrane | 3$B7o(B | ||
| Pd membrane | 3$B7o(B | ||
| CO2 separation | 2$B7o(B | ||
| forward osmosis | 2$B7o(B | ||
| Commercial Pd plating reagent | 1$B7o(B | ||
| $B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $BH/I=7A<0(B | |
|---|---|---|---|
| 33 | $B;THN$N(BPd$B$a$C$-;nLt$rMQ$$$?B?9& | Pd membrane Porous SUS tube Commercial Pd plating reagent | O |
| 34 | $BB?9&e$K@=Kl$7$?(BPd$BKl$N?eAG3H;6@-8~>e$r$a$6$7$?%7%j%+%i%$%HCf4VAX$X$N%"%k%+%j=hM}(B | Pd membrane Silicalite intermediate layer Alkali treatment | O |
| 35 | $BHf3SE*Bg$-$J:Y9&$r$b$DB?9& | Pd membrane Porous SUS support Intermediate layers | O |
| 39 | $BL55!!?M-5!%O%$%V%j%C%I%$%*%s%2%k$N%M%C%H%o!<%/9=B$@)8f$K4X$9$k4pACE*8!F$(B | membrane CO2 separation ionic liquid gel | O |
| 55 | $B%$%*%s1UBN@-%]%j%^! | Membrane CO2 separation Facilitated transport membrane | O |
| 97 | $BG.M65/AjJ,N%K!$K$h$k9bJ,;RB?9&Kl$NI=LL9=B$$N@)8f(B | membrane thermally induced phase separation surface structure | O |
| 98 | $BB?CJ<0Dc055U?;F)K!$rMxMQ$7$?1v?eG;=L%W%m%;%9$N8!F$(B | reverse osmosis brine concentration multistage process | O |
| 111 | $BM-5!%-%l!<%H$rMQ$$$?B?9&@-(BTiO2-ZrO2$BJ#9gKl$N:n@=$H9=B$I>2A(B | porous ceramic membrane TiO2-ZrO2 organic chelate | O |
| 117 | pKa$B$,0[$J$k%"%_%s4^M-%2%kN3;R$r@QAX$5$;$?Kl$N(BCO2$BF)2aN.B.$NI>2A(B | carbon dioxide membrane separation pKa | O |
| 122 | $B2 | forward osmosis sewage treatment membrane fouling | O |
| 164 | FO$BKl%W%m%;%9$KMQ$$$k29EYAjE>0\J* | forward osmosis draw solute phase transition | O |
(C) 2017 $B8x1W
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