$B:G=*99?7F|;~!'(B2015-01-20 21:42:24
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
draw solution | 2$B7o(B | ||
forward osmosis | 2$B7o(B | ||
Palladium membrane | 2$B7o(B | ||
internal concentration polarization | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
1 | $B@5?;F)KlK!$X$NMxMQ$r;X8~$7$?%]%j%"%_%s7O6nF0MO1U$NAO@=(B | Forward osmosis Draw solution Polyamine | O |
10 | $B%7%j%+%i%$%HAX$rCf4VAX$H$7$FF3F~$7$?B?9& | Palladium membrane Porous stainless steel silicalite | O |
11 | $BGQ1U$+$i$N%P%$%*%(%?%N!<%k$N?;F)5$2=J,N%$KMQ$$$k%7%j%+%i%$%HKl$ND4@=K!$N8!F$(B | Silicalite membrane Pervaporation Bio-ethanol | O |
12 | A$B7?%<%*%i%$%H$H%"%k%_%J$rJ#AX2=$7$FCf4VAX$r7A@.$7$?B?9& | Palladium membrane porous stainless steel support double intermediate layers | O |
52 | $B3J;R%\%k%D%^%sK!$rMQ$$$?1UE)$NKl:Y9&F)2a%7%_%e%l!<%7%g%s(B | Lattice Boltzmann method membrane permeation two-phase flow | O |
95 | $BA0=hM}$H$7$F$N@8J*@\?($m2a$,@:L)$m2aKl$K5Z$\$91F6A$NI>2A(B | Microfiltration Biological pre-treatment River water | O |
109 | $B8wG.JQ49$K$h$kF)2a@)8f$rL\;X$7$?G.1~Ez@-%]%j%^! | thermoresponsive polymer membrane gold nanoparticle | O |
118 | $B%$%*%s1UBN?eMO1U$N?;F)05$K4X$9$k4pACE*8!F$(B | ionic liquid membrane separation osmotic pressure | O |
124 | $B0[$J$k6nF0MO | forward osmosis draw solution internal concentration polarization | O |