$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
---|---|---|---|---|---|
F$B2q>l(B $BBh(B2$BF|(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B2<:d(B $B8|;R(B) | |||||
F201 | $B?75,J.L8G.J,2rK!$K$h$kCV497?%9%T%M%k%j%A%&%`%^%s%,%sJ#9g;@2=J*%J%NN3;R$N9g@.(B | Spray pyrolysis Lithium-ion battery Cathod | S-4 | 69 | |
F202 | $BG.J,2r2aDx$K$*$1$k8GBNG3NAN3;RFb$N05NO5sF0(B | pressure measurement thermal decomposition particle | S-4 | 223 | |
F203 | $BL5 | circulating fluidized bed powder dispersion Froude number | S-4 | 979 | |
(10:00$B!A(B11:20)$B!!(B($B:BD9(B $BCfN$!!JY(B) | |||||
F204 | $BBg>.Fs@.J,N3;R7O%I%i%U%H%A%e!<%VIU$-(BSpout-Fluid Bed$B$NN.F0FC@-(B | spout-fluid bed pressure fluctuation gas bypassing | S-4 | 29 | |
F205 | $B8:052aG.?e>x5$N.F0AX4%AgFC@-$K5Z$\$9A`:n>r7o$N1F6A(B | superheated steam fluidized bed drying porous particles | S-4 | 521 | |
F206 | $B8G5$N.F0AX$rMQ$$$?2HEE%7%e%l%C%@!<%@%9%HFb$N1vAG4^M-%W%i%9%A%C%/$NJ,N%(B | Fluidized Bed Home Electric Appliance Shredder Residue Gravity Separation | S-4 | 944 | |
F207 | $B8G1UN.F0AX$K$h$kL)EY:9J,N%(B | Fluidized Bed Solid Waste Sparation | S-4 | 155 | |
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $BN)85(B $BM:<#(B) | |||||
F208 | [$BE8K>9V1i(B] $BGQ4~J*%j%5%$%/%k$N$?$a$N4%<0Hf=EJ,N%5;=Q$N | fluidized bed waste gravity separation | S-4 | 189 | |
(14:40$B!A(B15:20)$B!!(B($B;J2q(B $BBgC+(B $B5H@8(B) | |||||
F218 | [$BE8K>9V1i(B] $B%;%a%s%H@=B$J,Ln$K$*$1$k;q8;%j%5%$%/%k5;=Q(B | $B%j%5%$%/%k(B $B%;%a%s%H(B $B>J%(%M%k%.(B- | S-4 | 71 | |
(15:20$B!A(B16:00)$B!!(B($B:BD9(B $B;3K\(B $BE0Li(B) | |||||
F220 | $B4IFb8G5$FsAjN.$K$*$1$kN3;R$N5sF0$HBSEE$KH<$&EE5$?.9f$N2r@O(B | Gas-solids pipe flow Particle charging Charge transfer | S-4 | 31 | |
F221 | AFM$B$rMQ$$$?HyN3;R$NEE>lCf$K$*$1$k@\?(BSEE$N2r@O(B | Atomic Force Microscope Contact Electrification Electric Potential | S-4 | 606 | |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $B>>:d(B $B=$Fs(B) | |||||
F222 | $BGQ4~J*7O3J;R;@AG$K$h$kC:2=?eAG=hM}$K4X$9$k8&5f(B | Lattice Oxygen Waste Metal Oxide Gasification | S-4 | 224 | |
F223 | Mechanochemical synthesis of Mg-Al-OH hydrotalcite | mechanochemical hydrotalcite synthesis | S-4 | 380 | |
F224 | $BD62;GH>H | ultrasonic disaggregation nano-sized crystalline particles | S-4 | 590 | |
F$B2q>l(B $BBh(B3$BF|(B | |||||
(9:20$B!A(B10:20)$B!!(B($B:BD9(B $B2CG<(B $B=cLi(B) | |||||
F302 | VOF$BK!$K$h$k(B3$BAjN.BNCf$N1UE)@8@.%7%_%e%l!<%7%g%s(B | emulsion VOF CFD | S-4 | 305 | |
F303 | $BN>C<$r5[<}JI$K;}$D(B1$B | Brownian motion Langevin equation one-dimensional diffusion | S-4 | 384 | |
F304 | DEM-CIP$BK!$K$h$k8GBNHyN3;R7|By1U$N4%Ag5sF0%7%_%e%l!<%7%g%s(B | DEM Drying CFD | S-4 | 75 | |
(10:20$B!A(B11:20)$B!!(B($B:BD9(B $BJ?Ln(B $BGnG7(B) | |||||
F305 | $B9bO'Fb$K$*$1$kJ4N3BN$N5sF0(B | blast furnace rigid plastic analysis mathematical model | S-4 | 320 | |
F306 | $BM7@1%\!<%k%_%j%s%0$K$*$1$kFbIt29EY$NB,Dj$HM=B,(B | Planetary ball mill Grinding DEM | S-4 | 89 | |
F307 | $BN3;R7BHf$NBg$-$$>r7o2<$K$*$1$kN3;R8!:w%"%k%4%j%:%`$N9bB.2=(B | Discrete Element Method Contact Detection Speed-up | S-4 | 81 | |
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $B5HED(B $B1Q?M(B) | |||||
F308 | [$BE8K>9V1i(B] $BJ4BN%7%_%e%l(B-$B%7%g%s$N$5$i$J$kH/E8$N$?$a$K(B | $BJ4:U(B $B%7%_%e%l(B-$B%7%g%s(B $B%a%+%N%1%_%9%H%j(B- | S-4 | 72 | |
(14:40$B!A(B16:00)$B!!(B($B:BD9(B $B1JEg!!Bg(B) | |||||
F318 | $BHyN3;R$N4IFbN.$l$K4X$9$k8&5f(B | fine particle flow structure DDS | S-4 | 921 | |
F319 | $BN3;R72$U$k$$J,$12aDx$K$*$1$kHyN3;RDL2a%b%G%k(B | passage probability percolation simulation | S-4 | 362 | |
F320 | $B<'5$J,N%5!$K$h$k(BFCC$BGQ?(G^:o8:$N3+H/Z2=(B | FCC Catalyst HGMS | S-4 | 15 | |
F321 | $BA!0]AX%U%#%k%?$rMQ$$$?47@-$K$h$kN3;R$NJ,5i(B | fibrous filter inertia classification | S-4 | 420 | |
(16:00$B!A(B17:20)$B!!(B($B:BD9(B $B2!C+!!=a(B) | |||||
F322 | $BEE>l0u2C7?$N?77??edA$K$h$kHyN3;R$N9b@:EYJ,5i(B | $BEE5$1KF08z2L(B $B?edA(B $B<><0J,5i(B | S-4 | 73 | |
F323 | $B<><0%5%$%/%m%s$K$h$k@VE%$NJ,5iFC@-(B | wet cyclone red mud classiffication | S-4 | 608 | |
F324 | $B1s?4J,N%5!$K$h$kHyN3;R$NJ,5i(B | classification centrifuge particle | S-4 | 468 | |
F325 | $BGX052<$K$*$1$k%*%j%U%#%9IU$-N.2<4IFb$NN3;R72$N5sF0(B | stand pipe packed bed flow pattern discharge rate | S-4 | 28 |