$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B $B!cN3;R!&N.BN7OJ,N%5;=Q$N?7$?$JD)@o!d(B | |||||
(10:00$B!A(B11:20)$B!!(B($B:BD9(B $BEDCf(B $B9'L@(B) | |||||
R104 | $B%3%m%$%IJq3g%2%k2=K!$rMQ$$$?GQ1U$N@6@!2==hM}(B | colloid gel expression | S-32 | 722 | |
R105 | $BKlMxMQ7?9ZAG=hM}%7%9%F%`$K$h$kCe?'GQ?e$NC&?'(B | membrane enzyme decolorization | S-32 | 632 | |
R106 | $BE`7kM;2rK!$K$h$k%(%^%k%7%g%s7O%3%m%$%I$NJ,N%@-G=(B | freeze-thaw emulsion separation | S-32 | 636 | |
R107 | $BD62;GH>H | Freeze Concentration Supersonic Radiation Solid Liquid Separation | S-32 | 918 | |
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $B5HED(B $BM5;V(B) | |||||
R108 | [$BE8K>9V1i(B]$B!!79 | tube settler lamella plate gravity settling | S-32 | 79 | |
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $B@n:j(B $B7rFs(B) | |||||
R113 | [$BE8K>9V1i(B] $B_I2a=u:^$N8=>u$H:#8e(B | filter aid diatomaceous earth perlite | S-32 | 336 | |
(13:40$B!A(B15:00)$B!!(B($B:BD9(B $BJR6M(B $B@?G7(B) | |||||
R115 | MBR$BMQ(BPTFE$BKl$N3+H/(B | PTFE MBR activated sludge | S-32 | 941 | |
R116 | $BCf6u;e@:L)_I2aKl$N8G1UJ,N%FC@-$K5Z$\$9_I2a;~4V$N1F6A(B | hollow fiber membrane filtration time activated sludge | S-32 | 474 | |
R117 | $BCf6u;e@:L)_I2aKl$N@->u$N0c$$$,M>>j3h@-1xE%$N_I2aFC@-$K5Z$\$91F6A(B | hollow fiber membrane pore size clogging | S-32 | 480 | |
R118 | $B9bEE2r | microfiltration electrolyte particle | S-32 | 1001 | |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BCfB<(B $B0lJf(B) | |||||
R119 | $BHsBP>N7?%G%W%9%U%#%k%?!<$K$h$k:Y6]7|By1U$N@:L)_I2a(B | depth filter microfiltration bacteria | S-32 | 318 | |
R120 | $B%]%jF};@@=%G%W%9%U%#%k%?!<$N3+H/(B | depth filter biodegradable poly(L-lactic acid) | S-32 | 321 | |
R121 | $B2D5U6E=8(B-$BB?CJD69b0505:q%7%9%F%`$K$h$k2 | ultrahigh-pressure expression reversible flocculation dewatering | S-32 | 635 | |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $B;TB<(B $B=E=S(B) | |||||
R122 | $B;@2=E4%9%i%j!<$N%1!<%/%l%9C&?eAuCV$N3+H/(B | filtration flowable slurry iron oxide | S-32 | 279 | |
R123 | $B4I7BJ}8~J,G[%/%m%^%H%0%i%U%#!<$K$*$1$k@8BN9bJ,;R$NJ,@O(B | Capillary chromatography Laminar flow Biopolymer | S-32 | 27 | |
R124 | $B%;%7%&%`O"B3Cj=P$N$?$a$N1U!98~N.7?1s?4Cj=PAuCV$N3+H/(B | Centrifugal Extractor Multistage Separation Counter-current Flow | S-32 | 1052 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B $B!cN3;R!&N.BN7OJ,N%5;=Q$N?7$?$JD)@o!d(B | |||||
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BH"ED(B $BM%(B) | |||||
R204 | $B%7%j%+%J%NN3;R$N2sJ,<0$*$h$SO"B3<0J,5iAuCV$N3+H/(B | classification electrophoresis fine particles | S-32 | 812 | |
R205 | $B>e8~N._I2a$K$*$1$k:.9g%J%NN3;R%1!<%/AX$NGmN%8z2L$K5Z$\$9;nNA>r7o$N1F6A(B | nanoparticle upward filtration filter cake | S-32 | 1031 | |
R206 | $BIT6Q0l%1!<%/BO@Q%b%G%k$K$h$kKlLL79 | inclined ultrafiltration filter cake nanocolloid | S-32 | 638 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B8~0f(B $B9/?M(B) | |||||
R207 | $BM6EE1KF0$rMQ$$$?J* | dielectrophoresis Clausius-Mossotti Factor quadrupole electrode | S-32 | 197 | |
R208 | $B7>AtEZ_I2a;D^V$+$i$N%l%"%a%?%k2s<}$rL\E*$H$7$?6bLV@QAX7?M6EE1KF0J,N%AuCV$N3+H/(B | dielectrophoresis diatomite filtration rare metal | S-32 | 252 | |
R209 | $BD>N.=E>v8rN.EE05$rMQ$$$?:Y9&@d1oHD7?M6EE1KF0AuCV$K$*$1$kJ,N%FC@-(B | dielectrophoresis separation | S-32 | 494 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B4dED(B $B@/;J(B) | |||||
R213 | $BF0J*:YK&$N%b%G%k$H$7$?(BW/O/W$B%(%^%k%7%g%s$NM6EE1KF05sF0$N8!F$(B | dielectrophoresis emulsion | S-32 | 407 | |
R214 | $BEE5$?;F)C&?eK!$K$h$kG;=L1xE%$NC&?eFC@-(B | filtration activated sludge electro-osmosis dewatering | S-32 | 433 | |
R215 | $BEE5$?;F)C&?eK!$K$*$1$kC&?e;nNA$NE,MQ@-$KBP$9$k | Solid-Liquid Separation Electro-Osmotic Dewatering Available Sludge | S-32 | 364 | |
$BBh(B3$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B%7%s%]%8%&%`(B $B!c>J%(%M%k%.!<$*$h$SFC | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B?9!!=( | |||||
R301 | $B>xN1Ec$K$*$1$kHtKwF1H | entrainment efficiency distillation | S-33 | 333 | |
R302 | $B%J%,%*%+!!%Q%C%-%s%0!!!V%9!<%Q!<(BH$B%Q%C%/!W!!(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= | Linear Flow High Operating Capacity High Liquid Hold | S-33 | 216 | |
R303 | $B%(%?%N!<%k(B+$B?e(B+$B%(%A%l%s%0%j%3!<%k7O$N5$1UJ?9U$NB,Dj$*$h$S>xN1$X$N1~MQ(B | vapor-liquid equilibrium Ethylene glycol extractive distillation | S-33 | 653 | |
(10:00$B!A(B11:20)$B!!(B($B:BD9(B $B>>ED7=8g(B) | |||||
R304 | $B8:057O(BHIDiC$B$K$h$k%(%?%N!<%kG;=L%W%m%;%9$N>J%(%MBP:v(B | Ethanol Distillation HIDiC Energy Saving | S-33 | 15 | |
R305 | $B>xN1%W%m%;%9(B"Compressor-Free HIDiC"$B$N>J%(%M%k%.! | Distillation heat-integration Energy-Saving | S-33 | 950 | |
R306 | $BFbItG.8r497?>xN1Ec$K$*$1$k:GE,G.8r49NLJ,I[(B | HIDiC Reversible Distillation Side Heat Exchanger | S-33 | 966 | |
R307 | $BFs=E4I7k9g7?>xN1Ec$N>J%(%M%k%.! | Three Component Distillation Coupled Column Energy Saving | S-33 | 16 | |
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $BC[>kMxI'(B) | |||||
R308 | [$BE8K>9V1i(B] $B:G6a$N>J%(%M%k%.!<>xN15;=Q(B -$B5;=Q3+H/$N8=>u(B- | Energy-saving distillation HIDiC DWC | S-33 | 63 | |
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $B>>ED7=8g(B) | |||||
R313 | [$BE8K>9V1i(B] $B4D6-6&@82=3X$H%3%W%m%@%/%7%g%s(B $B!<2=3X%W%i%s%H$O@8BV7O$rL\;X$9$N$+!)(B- | Co-production energy-saving chemical plant | S-33 | 228 | |
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $B | |||||
R315 | $B>xN1Ec$K$*$1$kEcFbAH@.$N5UE>8=>]$K$D$$$F(B | Distillation Internal Heat Integration Separation | S-33 | 53 | |
R316 | $B?bD>J,3d7?>xN1Ec$KBP$9$k?eNO3X$r9MN8$7$?2r@OK!$N3+H/(B | Dividing Wall Columns Hydrodynamics Simulation | S-33 | 429 | |
R317 | $B?bD>J,3d7?Cj=P>xN1Ec$NA`:nFC@-(B | Divided-Wall Column for Extractive Distillation simulation saving energy | S-33 | 473 | |
(14:40$B!A(B15:20)$B!!(B($B:BD9(B $BCf4d>!(B) | |||||
R318 | $BH?1~>xN1%W%m%;%9$N%@%$%J%_%C%/%7%_%e%l!<%7%g%s(B | Reactive distillation Dynamic simulation Process Intensification | S-33 | 312 | |
R319 | $B%P%C%A>xN1Ec$K$h$k(BIPA$B@:@=%W%m%;%9$N>CHq%(%M%k%.!<$K4X$9$k8!F$(B | batch distillation refinement simulation | S-33 | 506 | |
$BAm9gF$O@(B |