$B:G=*99?7F|;~!'(B2011-02-02 10:29:01
halogen replacement reaction (1$B7o(B) | ||||
---|---|---|---|---|
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
141 | $B%^%$%/%m%-%c%T%i%j! | 5-f | micro reactor phase transfer catalyst halogen replacement reaction | 12/7 14:00:57 |
HAZOP(Hazard and Operability Study) (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 10-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
668 | HAZOP$B2r@O>pJs$rMxMQ$7$?%U%)!<%k%H!&%D%j!<$N<+F0@8@.(B | 10-e | HAZOP(Hazard and Operability Study) FTA(Fault Tree Analysis) Risk Evaluation | 12/10 19:30:16 |
Heat integration (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
148 | Synthesis of optimal distillation sequences with heat integration and compressor addition using multiobjective optimization | 4-c | Heat integration Compressor addition Multiobjective optimization | 12/7 16:00:24 |
heat of immersion (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
700 | $BMOG^Cf$K$*$1$k%J%NN3;R$NJ,;6!&6E=8FC@-I>2A$rL\;X$7$??;DRG.B,DjK!$N3+H/(B | 12-d | nanoparticle heat of immersion dispersion | 12/10 21:01:06 |
Heat of solution (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
32 | $BMO2rG.$rMQ$$$??eOBJ*7OM-5!7k>=$NE>0\29EY$N?d;;(B | 12-g | Crystal Heat of solution Hydrate | 11/24 11:02:18 |
heat pipe (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
757 | $B%R!<%H%Q%$%W7?%R!<%H%9%W%l%C%@(B-$B$rMQ$$$?Nd5Q%7%9%F%`$NDcG.Dq932=$K$D$$$F(B | 2-a | heat pipe heat spreader thermal resistance | 12/12 13:44:48 |
Heat pump (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
176 | $B2=3X5[<}K!$K$h$k(BCO2$B2s<}%W%m%;%9$N>J%(%M%k%.!<2=8!F$(B | 13-g | Carbon capture and storage Amine Heat pump | 12/8 11:38:13 |
464 | Adsorption/desorption of water-zeolit pairs in the adsorption heat pump system for generating steam | 3-b | adsorption-desorption steam generation heat pump | 12/10 12:42:16 |
Heat spreader (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 11-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
247 | $BD6G.EAF3@\Ce%U%#%k%`$N3+H/(B | 11-c | Thermal problem Thermal design Heat spreader | 12/9 11:46:06 |
757 | $B%R!<%H%Q%$%W7?%R!<%H%9%W%l%C%@(B-$B$rMQ$$$?Nd5Q%7%9%F%`$NDcG.Dq932=$K$D$$$F(B | 2-a | heat pipe heat spreader thermal resistance | 12/12 13:44:48 |
Heat storage (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
121 | Performances of a MgO-expanded graphite packed bed reactor of chemical heat pump | 9-b | chemical heat pump expanded graphite Heat storage | 12/6 19:29:31 |
Heat Storage material (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
544 | $BB?9&BNC4;}7?(BCa(OH)2$B2=3XC_G.:`$K$*$1$k?eOB!&C&?eH?1~B.EY$N | 9-b | Chemical Heat storage Heat Storage material Reactivity | 12/10 15:55:31 |
heat transfer (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
149 | $B%a%?%s%O!<%I%l!<%HLO5<%3%";nNA$NG.EAF3EYB,Dj$HM[2rK!$K$h$kG.0\F0%b%G%k(B | 9-a | methane hydrate explicit method heat transfer | 12/7 16:25:28 |
517 | $B%<%*%i%$%H= | 9-b | Microwave heating Desorption Heat transfer | 12/10 14:44:49 |
heat-alkali treatment (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
402 | $BG.%"%k%+%j=hM}$K$h$k2DMO2=1xE%$NHy@8J*AQ2r@O(B | 7-g | sludge reduction heat-alkali treatment 16S rRNA | 12/10 08:38:04 |
Heating rate (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 3-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
132 | $B3lC:$N4xH/J,J|=PB.EY$NB,Dj$H$=$N4pACE*FC@-(B | 3-b | Pyrolysis Brown coal Heating rate | 12/7 12:02:05 |
Heating rate effect (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
508 | Critical Parameter for Scale up of Microreactor Synthesis: Heating Rate Effects | 5-f | Microreactor Scale up Heating rate effect | 12/10 14:19:33 |
heavy metal vapors (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-i (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
585 | Evaluation of HCl/SO2/H2O on Super-saturation of Heavy Metal Vapors in the Cooling Section of Flue Gas | 13-i | Super-cooling heavy metal vapors deposition | 12/10 17:05:48 |
hematopoietic differentiation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
89 | $BfuMMBN$r2p$7$?(BES$B:YK&$+$iB$7l44:YK&$X$NJ,2=M6F3%W%m%;%9$N:GE,2=$K4X$9$k8!F$(B | 7-e | embryonic stem cell hematopoietic differentiation hematopoietic stem cell | 12/3 14:30:08 |
hematopoietic stem cell (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
89 | $BfuMMBN$r2p$7$?(BES$B:YK&$+$iB$7l44:YK&$X$NJ,2=M6F3%W%m%;%9$N:GE,2=$K4X$9$k8!F$(B | 7-e | embryonic stem cell hematopoietic differentiation hematopoietic stem cell | 12/3 14:30:08 |
hepatic differentiation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
85 | $B%P%$%*?M9)4NB!3+H/$K8~$1$?%*%k%,%N%$%IG]M\K!$K$h$k4NJ,2=M6F3K!$NM-MQ@-I>2A(B | 7-e | embryonic stem cell hepatic differentiation hollow fiber | 12/3 11:45:07 |
Hepatocyte (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
67 | $B4N:YK&%^%$%/%m%Q%?!<%K%s%0G]M\$K$*$1$k:YK&%9%]%C%H%5%$%:$N8z2L(B | 7-e | Hepatocyte Micropattering culture Liver-specific function | 12/1 17:47:52 |
586 | $B^uN.%^%$%/%m%G%P%$%9$rMQ$$$?4N:YK&%9%U%'%m%$%IG]M\(B | 7-e | Spheroid Perfusion culture Hepatocyte | 12/10 17:06:56 |
hepatoma cell (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
697 | $B4NFC0[E*E> | 7-a | transcription factor hepatoma cell liver function | 12/10 20:53:43 |
hetero nucleation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
305 | $BHoJ$7??eAG5[B"J#9gN3;R$N:n@=$HFC@-I>2A(B | 12-c | hetero nucleation hydrogen absorption coating | 12/9 15:53:52 |
heteroconjugation of protein (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
227 | $B%A%m%7%s;@2=H?1~$rMQ$$$?0[ | 7-a | Tyrosine coupling reaction horseradish peroxidase heteroconjugation of protein | 12/8 23:18:09 |
Hexokinase (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
709 | $B%b%G%k@8BNKl$K$h$k(BHekixokinase$B3h@-$N@)8f(B | 7-b | Membranome Liposome Hexokinase | 12/10 21:22:45 |
HF-PES membrane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
312 | Surface modification of PES membrane for antibacterial surface design | 4-a | Surface functionalization HF-PES membrane Zwitterionic monomer | 12/9 16:36:20 |
HIDiC (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (2$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
2 | 3$B@.J,7O>xN15;=Q$NJ,N%FC@-$H>J%(%M%k%.! | 4-c | 3-component Distillation HIDiC DWC | 11/8 14:25:22 |
201 | $B%R!<%H%]%s%W%"%7%9%H$K$h$k%P%C%A>xN1$N>J%(%M%k%.!<2=(B | 4-c | Batch distillation HIDiC Energy saving | 12/8 18:38:31 |
High density (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
35 | $BN3;R!&N.BN%W%m%;%9It2q%7%s%]%8%&%`>^(B($B>)Ne>^(B) $B;0Ec<0Bg7?=[4DN.F0AX$N3+H/(B (1)$B9bB.9bL)EY1?E>;~$NN.F0FC@-(B | 2-c | Circulating Fluidized Bed Flow behavior High density | 11/24 15:24:36 |
High encapsulation efficiency (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
145 | $BFs=E4I7?@EEEJ.L8K!$K$h$k%j%s;i | 12-b | Coaxial electrospray Giant phospholipid vesicle High encapsulation efficiency | 12/7 15:12:06 |
high flux dialyzer (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
430 | $B9b@-G=%@%$%"%i%$%6Fb$G@8$8$kFbIt_I2a8=>]$N7lN.NL0MB8@-$N8!F$(B | 7-e | internal filtration rate high flux dialyzer fouling | 12/10 11:07:08 |
High Liquid Hold (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
283 | $B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= | 4-c | Linear Flow High Operating Capacity High Liquid Hold | 12/9 14:51:17 |
High Operating Capacity (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
283 | $B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= | 4-c | Linear Flow High Operating Capacity High Liquid Hold | 12/9 14:51:17 |
328 | CO2$B$N5[<}!&:F@8$K8z2LE*$J5,B'= | 13-g | Linear Flow High Operating Capacity Capillary Action | 12/9 17:23:10 |
High Pressure (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
13 | $B5$K"Ec$NN.F0MM<05Z$S%,%9%[!<%k%I%"%C%W$K5Z$\$91?E>05NO$N1F6A(B | 2-d | Bubble Columns High Pressure Gas Holdup | 11/10 18:20:32 |
317 | $B%"%s%b%K%&%`1v$N9b05>=@O$K$*$1$k3KH/@805NO(B | 12-g | crystallization nucleation high pressure | 12/9 16:45:18 |
High pressure CO2 (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
295 | $B9b05(BCO2$BCf$G$ND62;GH%-%c%S%F!<%7%g%s$rMxMQ$7$?N3;R$NJ#9g2=$HB?9& | 8-e | Ultrasonic irradiation High pressure CO2 Porous glass | 12/9 15:32:34 |
High Purity Silica (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
156 | $B%F%H%i%"%k%3%-%7%7%i%s$N5$Aj2C?eJ,2r$K$h$k9b=cEYHyJ4Kv%7%j%+$N9g@.(B | 2-f | Gaseous Phase Hydrolysis Tetraalcoxysilane High Purity Silica | 12/7 19:34:14 |
high temperature (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
596 | $BCf6u;eKl%3%s%?%/%?!<$rMQ$$$?(BCO2$B2=3X5[<}%W%m%;%9$N9b292=$K$h$k9b8zN(2=(B | 13-g | CO2 absorption hollow fiber membrane high temperature | 12/10 17:15:33 |
High Temperature and High Pressure Water (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
473 | $B9b299b05?e(B-$B%^%$%/%m%j%"%/%?!<$rMQ$$$?NkLZ%+%C%W%j%s%0H?1~(B | 5-f | High Temperature and High Pressure Water microreactor Suzuki coupling reaction | 12/10 13:03:59 |
High Temperature/Pressure (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
572 | $BD>@\DLEE>.7?%,%92=H?1~AuCV$rMQ$$$?9b299b052<$G$N@PC:$N%,%92=B.EYB,Dj(B | 9-c | Coal Gasification Directly Heated Reactor High Temperature/Pressure | 12/10 16:53:38 |
high viscous fluid flow (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
333 | $B%,%i%9MOM;O'$N?tCM2r@O$H$=$N8!>Z(B | 2-a | MPS method glass melter high viscous fluid flow | 12/9 17:33:38 |
high-pressure and high-temperature (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
159 | $B9b299b05Fs;@2=C:AG$rMQ$$$kG"AG2=9gJ*$N9g@.(B | 8-d | carbon dioxide high-pressure and high-temperature urea | 12/7 22:15:58 |
high-purified solvent (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
515 | $B%]%j%$%_%IKl$K$h$kMO:^$N9bC&?e@:@=(B | 4-a | high-purified solvent azeotropic distillation nitorogen recycle parge | 12/10 14:41:51 |
high-temperature and high-pressure aqueous solution (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
690 | $B%^%$%/%m%A%c%M%k$rMQ$$$?9b299b05?eMO1U$NA4<+F0(BpH$BB,Dj%7%9%F%`$N3+H/(B(1) | 8-b | high-temperature and high-pressure aqueous solution automatic measurement system pH | 12/10 20:44:25 |
higher order structure (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
612 | $B?eMO@-6bB0%J%NN3;RB8:_2<$K$*$1$k%?%s%Q%/ | 12-a | nanoparticles protein higher order structure | 12/10 17:52:22 |
hollow fiber (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
85 | $B%P%$%*?M9)4NB!3+H/$K8~$1$?%*%k%,%N%$%IG]M\K!$K$h$k4NJ,2=M6F3K!$NM-MQ@-I>2A(B | 7-e | embryonic stem cell hepatic differentiation hollow fiber | 12/3 11:45:07 |
hollow fiber membrane (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
5 | 3D Modeling and Simulation of a Hollow fiber Membrane Module for IPA Purification from Water | 4-a | hollow fiber membrane membrane module modeling | 11/8 15:34:17 |
596 | $BCf6u;eKl%3%s%?%/%?!<$rMQ$$$?(BCO2$B2=3X5[<}%W%m%;%9$N9b292=$K$h$k9b8zN(2=(B | 13-g | CO2 absorption hollow fiber membrane high temperature | 12/10 17:15:33 |
hollow silica particle (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
326 | $BCf6u%7%j%+N3;R$N%j%]%=!<%`%F%s%W%l!<%H9g@.$K5Z$\$9%j%]%=!<%`I=LLFC@-$N1F6A(B | 12-a | hollow silica particle liposome surface properties | 12/9 17:15:14 |
Homogeneous precipitation method (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-k (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
223 | $B?eMO@-%1%$AG2=9gJ*$rMQ$$$?6Q0lD@EBK!$K$h$k(BZn2SiO4:Mn2+$B7V8wBN$N9g@.(B | 12-k | Water soluble silicon compound Homogeneous precipitation method Zn2SiO4:Mn2+ phosphor | 12/8 21:42:29 |
honeycomb (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 28-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
39 | [$B0MMj9V1i(B]$B5[CeK!$K$h$kGS%,%9Cf$N(BCO2$B=|5n!&G;=L%7%9%F%`$N:GE,2=$HN.F0$N1F6A(B | 28-b | adsorption CO2 honeycomb | 11/25 17:19:16 |
669 | $B%H%j%A%&%`=|5n%7%9%F%`$X$N%O%K%+%`?(G^$NE,1~(B | 5-a | tritium honeycomb catalyst | 12/10 19:35:09 |
horseradish peroxidase (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
227 | $B%A%m%7%s;@2=H?1~$rMQ$$$?0[ | 7-a | Tyrosine coupling reaction horseradish peroxidase heteroconjugation of protein | 12/8 23:18:09 |
hot compressed water (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
514 | $BG.?eN.DLH?1~$K$h$k%P%$%*%^%9$+$i$N%0%k%3!<%92s<}(B | 9-c | glucose cellulose hot compressed water | 12/10 14:38:36 |
hot gas desulfurization (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
106 | Regeneration Characteristics of Used Molten Alkali Carbonates for Hot Gas Desulfurization in Gasification Process | 9-a | hot gas desulfurization regeneration characteristic molten alkali carbonates | 12/6 11:26:38 |
Hot-Compressed Water (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
577 | $B%1%J%U7T?DIt$N2C05G.?e$H9ZAG=hM}$K$h$kE|2=(B | 9-c | Kenaf Core Biomass Hot-Compressed Water | 12/10 16:59:54 |
Hsp70B' promoter (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
680 | $B29G.M6F37?0dEA;R<#NE$N$?$a$N%O%$%V%j%C%I%W%m%b!<%?!<%7%9%F%`$N3+H/(B | 7-a | Tet-system Hsp70B' promoter Hyperthermia | 12/10 20:03:43 |
humidification (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
762 | $BCf6u;eF)<>KlEk:\$K$h$k<><0%G%7%+%s%H6uD45!$N2C<>@-G=I>2A(B | 9-f | humidification desiccant Air conditioning | 12/13 16:10:15 |
hybrid (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
190 | $B?eMO@-&P6&Lr7OM-5!J,;R(B / $BL55!%O%$%V%j%C%I7k>=$K$*$1$kH/8wFC@-$NI>2A$H$=$N@)8f(B | 12-g | hybrid phosphorescence potassium sulfate | 12/8 16:56:51 |
hybrid membrane (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
322 | BEA$B%<%*%i%$%HKt$O(BMCM-41/$BM-5!9bJ,;R%O%$%V%j%C%IKl$NF)2aJ*@-(B | 4-a | hybrid membrane mesoporous silica gas separation | 12/9 17:03:29 |
Hydrate (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-g (2$B7o(B), 12-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
32 | $BMO2rG.$rMQ$$$??eOBJ*7OM-5!7k>=$NE>0\29EY$N?d;;(B | 12-g | Crystal Heat of solution Hydrate | 11/24 11:02:18 |
308 | $B%O%$%I%l!<%HK!$K$h$k(BCO2$BJ,N%2s<}5;=Q$N8!F$(B | 13-g | carbon dioxide hydrate separation&capture | 12/9 16:03:19 |
400 | $BO"B3;n83AuCV$rMQ$$$?%O%$%I%l!<%HK!$K$h$kFs;@2=C:AGJ,N%5;=Q$N3+H/(B | 13-g | carbon dioxide hydrate gas separation | 12/10 08:25:36 |
Hydrate Slurry (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 2-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
202 | $B2sE>McYxYB$K$h$k?eOBJ*%9%i%j! | 2-b | Impeller Agitation Hydrate Slurry Particle Diameter | 12/8 18:39:52 |
Hydriodic acid (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
419 | $B%$%*%s8r49Kl$rMQ$$$?%h%&2=?eAGG;=L$K$*$1$kM"N($N29EY0MB8@-(B | 4-a | Cation exchange membrane Hydriodic acid transport number | 12/10 10:13:47 |
hydrocarbon decomposition (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
356 | $B%+!<%\%s%"%m%$C4;}(BNi$B?(G^$NC:2=?eAGJ,2rFC@-(B | 9-c | Ni Catalyst Carbon alloy hydrocarbon decomposition | 12/9 18:44:58 |
Hydrocarbon polyelectrolyte (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 9-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
119 | $BC:2=?eAG7OEE2r2A5Z$S8GBN9bJ,;R7AG3NAEECS?(G^AX$N:GE,2=(B | 9-e | PEFC Hydrocarbon polyelectrolyte Polymer properties | 12/6 18:47:34 |
hydrocarbon separation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
573 | Na$B7?(BZSM-5$BKl$X$NC:2=?eAG5[CeFC@-$N8!F$(B | 4-a | ZSM-5 membrane hydrocarbon separation adsorption property | 12/10 16:54:26 |
Hydrodenitrogenation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
579 | $B%i%$%H%5%$%/%k%*%$%kCf$NCbAG2=9gJ*$NH?1~@-$N2r@O(B | 5-a | Hydrodenitrogenation Kinetic analysis Light cyclic oil | 12/10 17:00:29 |
Hydrodeoxgenation (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
578 | $B%8%c%H%m%U%!$N?eAG2==hM}?(G^$N3+H/(B | 5-a | Jatropha oil Hydrodeoxgenation Isomerization | 12/10 17:00:28 |
hydrogel (6$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-e (4$B7o(B), 12-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
185 | $BE`7k(B-$BM;2r$K$h$j%2%k2=$9$k%-%H%5%sM6F3BN$ND4@=$*$h$SFC@-I>2A(B | 7-e | chitosan hydrogel | 12/8 15:31:26 |
254 | $B4629@-%R%I%m%2%k$+$i$N%?%s%Q%/ | 12-f | N-isopropylacrylamide hydrogel release rate | 12/9 12:22:12 |
381 | $B%^%$%/%mN.O)$rMQ$$$?LS;e6L>u%O%$%I%m%2%kN3;R$N9g@.$H:YK&G]M\C4BN$H$7$F$N1~MQ(B | 7-e | hydrogel alginate microfluidic device | 12/9 21:25:09 |
448 | $BA}?#0x;R$H;iKC44:YK&$r4^$`B?E|M6F3BNMO1U$NBNFb$G$N%2%k2=$K$h$k7l4I4^M-AH?%9=C[(B | 7-e | tissue engineering stem cell hydrogel | 12/10 11:44:11 |
561 | $BE`7k4%Ag%O%$%I%m%2%k$N:n@=$H%?%s%Q%/ | 7-h | hydrogel microencapsulation enzyme | 12/10 16:39:58 |
587 | $B%^%$%/%m%b!<%k%G%#%s%0$rMxMQ$7$?%Q%?!<%s2=%O%$%I%m%2%k:`NA$N:n@=$H1~MQ(B | 7-e | hydrogel micromolding tissue engineering | 12/10 17:07:36 |
hydrogen (7$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (2$B7o(B), 1-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
16 | $B6bB0Cf4VAX$rMxMQ$7$?9bBQ5W@-%Q%i%8%&%`GvKl$N:n@=(B | 4-a | palladium membrane hydrogen separation | 11/11 21:28:21 |
79 | $BJ,;RF0NO3X%7%_%e%l!<%7%g%s$K$h$k?eAG%O%$%I%l!<%HFb$N?eAG3H;65sF02r@O(B | 1-a | THF hydrogen MD | 12/2 17:50:34 |
336 | $B<><0J4:U$H2CG.$K$h$k%;%k%m!<%9$+$i$N?eAGH/@8(B | 2-f | cellulose hydrogen milling | 12/9 17:52:10 |
364 | $B?eAG@=B$MQ?(G^0lBN2=%b%8%e!<%k$N3+H/(B | 5-d | hydrogen membrane catalyst | 12/9 19:18:59 |
412 | $B:Y9&Fb= | 4-a | Gas separation membrane Hydrogen Palladium | 12/10 09:54:46 |
511 | $B%0%j%;%j%s$N?e>x5$2~ | 9-a | glycerin steam reforming hydrogen | 12/10 14:29:26 |
633 | $B<+N)7?(BH2-PSA$B$N(BDSS$BFC@-$N8!>Z(B | 9-c | Hydrogen PSA DSS | 12/10 18:30:51 |
hydrogen absorption (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-c (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
305 | $BHoJ$7??eAG5[B"J#9gN3;R$N:n@=$HFC@-I>2A(B | 12-c | hetero nucleation hydrogen absorption coating | 12/9 15:53:52 |
Hydrogen Sulfide Removal (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
425 | $BB?9& | 4-e | Iron oxide Sulfur Dioxide Removal Hydrogen Sulfide Removal | 12/10 10:53:18 |
Hydrogen Tank (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 3-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
387 | $B9b05?eAG5^B.= | 3-b | Hydrogen Tank Fast Filling Numerical Simulation | 12/9 22:40:52 |
hydrogenation (2$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-d (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
171 | Selective hydrogenation of dinitrile to aminonitrile in supercritical carbon dioxide | 8-d | Supercritical carbon dioxide hydrogenation adiponitrile | 12/8 10:31:29 |
362 | $BC4;}M-5!6bB0:xBN?(G^$N%7%j%+HoJ$$*$h$S$=$NH?1~FC@-(B | 5-a | Organometallic complex Silica coating Hydrogenation | 12/9 19:14:19 |
hydrolysis (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-e (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
175 | $B%A%?%K%"HyJ4$N5$Aj9g@.(B | 5-e | Titanium Tetraisopropoxide gas phase hydrolysis | 12/8 11:24:46 |
hydrophobic interaction (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 12-j (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
369 | $BAB?e4p$rF3F~$7$?%$%*%s@-4629@-%]%j%^!<$NE>0\5sF0$H7|ByN3;R$N05L)$X$N1~MQ(B | 12-j | thermosensitive polymer hydrophobic interaction compaction | 12/9 19:55:53 |
hydrophobic ligand (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
742 | $B%"%k%-%k:?$rF3F~$7$?AB?e2=4^CbAGB?:BG[0L;R$h$k=E6bB0J,N%(B | 4-f | extraction nitrogen donor hydrophobic ligand | 12/10 22:18:37 |
Hydrophobic organic pollutants (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
34 | $BAB?e4p4^M-9bJ,;R6E=87O$N@_7W$H?eCfAB?e@-M-5!1x@wJ* | 13-b | Hydrophobically modified polymers Hydrophobic organic pollutants Removal | 11/24 13:52:12 |
Hydrophobically modified polymers (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 13-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
34 | $BAB?e4p4^M-9bJ,;R6E=87O$N@_7W$H?eCfAB?e@-M-5!1x@wJ* | 13-b | Hydrophobically modified polymers Hydrophobic organic pollutants Removal | 11/24 13:52:12 |
Hydrothermal (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
469 | $BH>2sJ,<0H?1~4o$rMQ$$$?1v4p@-G.?e$K$h$k%]%jF};@$N2r=E9gB.EY$NB,Dj(B | 8-f | Hydrothermal Depolymerization Poly(lactic acid) | 12/10 12:53:20 |
712 | $B%a%A%l%s%8%U%'%N!<%k$rMQ$$$?%j%0%N%U%'%N!<%k%b%N%U%'%N!<%k2=$N>r7o8!F$(B | 5-g | Lignophenol Monophenol Hydrothermal | 12/10 21:30:58 |
732 | Synthesis of cobalt nanoparticles via hydrothermal reduction process at supercritical condition and its thermodynamic analysis | 8-e | supercritical hydrothermal SRK EOS | 12/10 22:00:08 |
Hydrothermal reaction (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-g (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
206 | $B7\1)LS$*$h$SCc3L$r86NA$H$7$?9b299b05H?1~$K$h$k1U>u;tNA2ACM$N@-G=I>2A(B | 8-f | Liquid feed Hydrothermal reaction Animal examination | 12/8 18:52:10 |
564 | $B?eG.=hM}$K$h$k%3!<%s%3%V$+$i$N%-%7%m%*%j%4E|@=B$(B(2) | 8-d | hydrothermal reaction biomass xylooligosaccharide | 12/10 16:44:48 |
756 | $B%j%0%N%;%k%m!<%97O%P%$%*%^%9$N?eG.E>2=$K4X$9$k8&5f(B | 5-g | Biomass Hydrothermal Reaction Separation | 12/12 13:28:35 |
Hydrothermal synthesis (3$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 8-e (2$B7o(B), 12-i (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
297 | $BD6NW3&?eG.K!$K$h$k(BEu$B%I!<%W%$%C%H%j%"%J%NN3;R$N9g@.(B | 8-e | Hydrothermal synthesis Nanoparticle Phosphor | 12/9 15:34:50 |
458 | 2$B | 12-i | ZnO nanorod hydrothermal synthesis XAFS | 12/10 12:28:51 |
502 | $B9b299b05?eCf$K$*$1$k(Bp$B7?F)L@;@2=J*H>F3BN(BCuAlO2$B$NO"B3?eG.9g@.(B | 8-e | Hydrothermal synthesis CuAlO2 semi conductor | 12/10 14:08:57 |
hydrothermal treatment (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
147 | $B?eG.=hM}$r;\$7$?%W%i%:%^MO | 4-a | hydroxyapatite plasma spraying hydrothermal treatment | 12/7 15:46:36 |
hydroxyapatite (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 4-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
147 | $B?eG.=hM}$r;\$7$?%W%i%:%^MO | 4-a | hydroxyapatite plasma spraying hydrothermal treatment | 12/7 15:46:36 |
Hyperthermia (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
680 | $B29G.M6F37?0dEA;R<#NE$N$?$a$N%O%$%V%j%C%I%W%m%b!<%?!<%7%9%F%`$N3+H/(B | 7-a | Tet-system Hsp70B' promoter Hyperthermia | 12/10 20:03:43 |
hyperthermophilc laccase (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-b (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
45 | $BD6BQG.@-(BLaccase$B$rMQ$$$?%P%$%*%+%=!<%I$N3+H/(B | 7-b | biofuel cell biocathode hyperthermophilc laccase | 11/26 17:30:15 |
Hyphal growth (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 7-a (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
42 | Growth Kinetics of Monascus Ruber on Rice Agar | 7-a | Monuscus Hyphal growth Glucosamine | 11/26 14:43:41 |
hysteresis loss heating (1$B7o(B) | ||||
$B$3$N%-!<%o!<%I$,$h$/;H$o$l$F$$$k%7%s%]%8%&%`!&9V1iJ,N`!'(B 5-f (1$B7o(B) | ||||
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | | |
463 | $B6/<'@-N3;R$N%R%9%F%j%7%9B;G.$rMxMQ$7$?9ZAGH?1~B%?JK!$N3+H/(B | 5-f | enzyme magnetic particle hysteresis loss heating | 12/10 12:41:52 |