Korean Chemical Engineering Research
전체 글
(2) ÜÍQ OYä ÆQË« @ æ2 Ê~É Hô-) í Ñ Âj2 s Y×Jk³ Æ G. OYäo ä« ,}æ2 8 äí ¡dõ îûO ¤ À´ ²«´ s zôK ÊF ä, Ñ ,}æÉk,
(3) Í kÎ o Îõ fGÊ2 ä, z=Q ³K QÆGÊ à ¯ Ê~É Hô-)õ »És ¤ À É. @ æ2 Ê~É Hô-) 9 ,
(4) Jo äHYí O
(5) Q OYä FtÑ ¶ ÍGk, ,ªJ ã2 Ýãf MMAõ ÍGñ ¬Q ¤ ÀÉ. Abstract − Experimental researches on the preparation of porous polymeric monoliths in supercritical carbon dioxide have been performed and the effects of monomer and polymerization parameters on the physical properties of the monolith prepared were examined. Polymerizations were carried out in the high pressure stainless steel reactor with sapphire window to show the phase change during the polymerization reaction, and continuous and dry porous monolithic polymer could be obtained. The specific surface area of monolithic polymer increased with monomer contents in reaction mixture and reaction pressure. The Rockwell hardness could be enhanced by the addition of co-monomer MMA in reaction mixtures. Key words: Porous Polymeric Monolith, Supercritical, Carbon Dioxide. 1.. C «. ¸Ñ [´Ë
(6) ñ6 õg¤« Ê~É Y ê Íà ~tÑ ð»ª Kõ «ÄK ΤK õg êËs ÝÊGD QÊG [3-7]. « ~t õg2 𻪠«d!Ñ ¬K Ê~É Ä gÑ îK õg, Ê~É Y Ú ß DgÑ îK õg, Ê~É 9Ã(bead) 2 § ½É fÆÑ îK õg -Ê à Ê~ É fÆÑ îK õg Ù« ?Íõ «PÊ À. Rindfleisch Ù[8]o 𻪠«d!Ñ ¬K Ê~ÉË Ägõ Æ K õgÑ 9 Ê~ÉË ð»ª «d!Ñ ¬K Äg 2 Ê~Éõ dGM÷(fluorinating) Ê~É ? 1(backbone) Ñ bs ÍG
(7) ÍQ ¤ ÀÊ ÝÊK à À. O’Neill Ù[9-10]o ð»ª Ñ siloxane ªù
(8) Ë ~ OYs Æ Gñ ½É _ DgQ ½É DgÑ îK õg êõ è,K à ÀÊ, Galia Ù[11]o 9v ªù
(9) Ë ~ O YÑ ¬g ÝÊK à À. Cooper Ù[12]o 𻪠«d!õ «ÄGñ Ê ÍGY s ä2 Ê~É Â§½Éõ fÆG2 Y×s }Gñ, ä HYíÑ 8_fõ ÍG
(10)
(11) §K ½ÉÍ fÆæÊ ¿DQ ½ 1990. 𻪠Kº ÊK»ªY « Ftê 5Ñ ÊéG
(12) D ê K K eª¤, Y Ù Mí s äÊ U ê 97K Êõ Í(2 D·U
(13) Kõ SK[1-2]. 𻪠KÍ ¤ HYí O U_ ~Ñ ¬Gñ >J¯ ~-Dts ÷2 Ù U«K ùòHJ Ms ä22 Yo 1ÖMz <s ÀÉ k÷, 1970¸¬Ñ [´Ë
(14) ÆñQ ¡dÑ Î½´ 𻪠K à_o _ÊdH, R\, H -Ê Ñw( Æ ÙÑ Y³ K Ä ÍD s (r Y0J¯ ¬ à_k³ ¬&æD QÊG. 𻪠K D¬o o Ägt, I YQ Ê eª¤³ ¯K Kñ z· Ùê ço 𻪠K ßYs «ÄG2 D¬³, DÊ ä Ú ~g, , _d, ¤, ô, QÆ, §_ Ù M HÇ dHà_Ñ D¬J ´sÞs gO ¤ À2 *³Ò D¬³ ?IçÊ À. † To. whom correspondence should be addressed. E-mail: [email protected] 21.
(15) 㧺ö? R. 22. ~¯2 8_f Ñ ¿j s ç22 as ÝÊG. LeleQ Shine Ù[13]o 𻪠Ê~É ÄUs H§îs 0Gñ è Qÿ2 ör(RESS)k³ Ê~É Â§ ½Éõ fÆG2 õgõ }K à À. CooperQ Holmes[14]2 𻪠KÑ Ñ Ägæ2 Í(
(16) õ ÄGñ ð»ª Ñ à Ê~Éõ fÆG2 Y×s }Gñ, ä HYí O
(17) Í ÍO¤´ @ æ2 à Ê~É Æ)« jÊg(Ê §à ¿DÍ Ê4 9 ,
(18) J « ÍK2 õg êõ ÝÊG. 𻪠Kõ «ÄGñ à Ê~É monolithõ fÆGD .g2,
(19) 2 𻪠«d!Ñ ¬K ÄgÍ ¿Ê @ æ2 Ê~É2 ÄgÍ Jo í0s >K. >ê
(20) õ í QfQ Wÿ ÊF äDÑ Ê ð»ª =Ñ Ê~É Y ä s ,}Qÿ
(21) 𻪠ÄUÑ ¬K ÄgÍ Jo Ê~É í0« @ ê. « Ê~É í0o ßG
(22) ½É k³ 𻪠K Ñ æ
(23) ³ 4Gñ à Ê~É monolithÍ @ æ 2 ak³ <s À[15-17]. á õgÑ2 𻪠«d!õ Äk³ ÄGñ ¿³K Ö) column £M í0[18-19], D 2 KD Äk ñê k Ùk³ lÄæ´ àÆJ ÍjÍ o à Ê~É monolithõ f ÆG2 Y×J õgõ }G.
(24) ÜÍQ ÆÊ¡¤Ë« @ æ2 Ê~É monolith í Ñ Âj2 s Æ GÊ, 𻪠Kõ «ÄGñ à Ê~Éõ fÆG2 à_Ñ îK MäJ¯ Æ õ G. 2.. / . /ð£ á õgÑ2
(25) Q OYä íQf Ú ð»ª «d! õ ÄGñ à Ê~É monolithõ fÆGD .Gñ Fig. 1Ñ ÷ àQ ço 𻪠OYä ßjõ fÊG. 𻪠OYä ßj2 «d! Y1
(26) , I5¤Æ, ÊFÄ hand pump, ]5¤Æ Ú äD -Ê 5Q Ft ÆQD Ù z ß 9³ g æÉ. Î ß9Ëo 1/8" ÊFÄ stainless îk³ õæÉ k, 1®K ÞÑ ÷ 1 Ú 8M-s jG. Ä
(27) 66 ml äD2 ÊF äs ¤}O ¤ À´ stainless steel³ f澃 k, @ ê monolithõ ò ¬³ ¡¤O ¤ À´ \Ñ ñ6 õ jG. ½g ä¬\ ñ6Ñ2 ä« ,}æ2 8 z ¡dõ îûO ¤ À´ sapphire windowõ zôG. ä D ½gÑ2 quick connectorQ õ jGñ äDõ ÍF = Ñ OYä ßj³z j ~-, ßôO ¤ À´ G. 2-2. Monolith£ g» Z Ïh á õgÑ2
(28) ³ TRM(trimethylol propane), EDMA(ethylene glycol dimethacrylate), DVB(divinyl benzene)õ, OY íQf³2 AIBN(2,2'-azobis (isobutyronitrile))s, OY Äk³2 𻪠«d! õ ÄGñ à Ê~É monolithõ fÆG. -Ê @ æ 2 monolith õ ¬QÿD .g 1®K ÎÑ2 à
(29) ³ MAA(methacrylic acid 2-diethyl aminoethyl ester)õ ÄG. Sapphire windowÍ zôê ÊF äDÑ Y Ñ ÄO
(30) , íQfõ £MGÊ OYä ßjÑ ßôK. äDQ OYä 2-1.. ¤@¤ C43× C1 2005 2. Fig. 1. Schematic diagram of experimental apparatus. 1. CO2 bomb 17. Pressure gauge 2. Valve 18. Vent 3. Cooler bath 19. Quick connector 4. Hand pump 10. Check valve 5. 1/8" tube 11. Reactor 6. Safety valve 12. Water bath. ßj z õ fMGD .g «d!õ Ik³ 15~ Ñ 1 {, ÊFÄ hand pumpõ ÄGñ äD z Ft s »ªFt « (100 bar)k³ ÍFK. äD ?. õ 4 äD z Fts K(K =Ñ quick connectorõ ÄG ñ äDõ OYä ßj³z ~-K. ~-ê äDõ ñ6 d Ë´ ä HYí« è³Gj HYæ´ T4(2 as sapphire windowõ 0Gñ e¯K. äDõ Q OYä ßjÑ ßôG Ê, ÊFÄ hand pumpQ ]5 ¤Æõ ÄGñ äD 5Q F ts òG2 =³ ÆQK. Sapphire windowõ 0Gñ äD z ¡dõ îûG
(31) O Y äs ,}Q. 20QÑ « äQ á äDõ 40 C³ ÎQÿÊ, äD zQ OYä ßj «d!õ gõ 0Gñ ¾ Q. «d!Í UM¾ æ
(32) äD \ ñ6õ T´ @ ê Ê~É monolithõ äDÑ ¡¤K. fÆê Ê~É monolith2 MÉ Â (SEM)ê 9 ,
(33) J +_ ßj(BET)õ ÄGñ í-J U s Æ GÊ, DªJ 2 Rockwell ªõ ÄGñ +_G. 9 ,
(34) J +_QÑ2 Qs ~GÑ K ,
(35) J Íõ ö(G D .g, @ ê Ê~É monolithõ 2 mm « ¿D³ ~GK á BETõ ÄGñ +_G. á õgÑ fÆK à Ê ~É monolithÍ ùÑ kÎ uK as Ý8Gñ, Ms- MÑ Q0 Dà ¤~s èGD Ò acetonek³ ¬K á 120 CÑ 24QÑ 8 M s-G. o. o. 3.. ûG Z +{. 3-1. /@| monolith£ <
(36)
(37) ÜÍQ , Y ä Ft Ú 5, Y ä QÑ Ù s ¡dQÿ
(38) ð»ª Ñ à Ê~É monolithõ fÆG 2 Y×s }K ê, ä HYí O
(39) Í 10% «G¯ Îõ fGÊ2 á õgÑ >K HÇ YׯQÑ äD.
(40) 𻪠«@õ «ÄK à Ê~É Monolith fÆ. z =Q ³K + à Ê~É monolithõ »s ¤ ÀÉ. fÆê monolith z s ÷Ê À2 Fig. 2õ Ý
(41) ,
(42) Í Ã ÎÑ2 äD z =Q ³K ò? monolithÍ fÆæ÷,
(43) Í Êo Î(>10%)Ñ2 ÍÒ) z~« ~-ê monolithÍ fÆæÉ. «6K o ð»ª Ñ Ê~ÉË« @ æ2 ê_s ]gÝ
(44) g« ÍDG. OYä« ,}öÑ ¶ 𻪠«d!Ñ Äg Í Jo Ê~ÉËo ßG
(45) æ´ 1ó ½Éõ GÊ, « Ë« ª ßG
(46) ³ YGñ monolithõ Gj ê. « ê_Ñ
(47) Í (÷jj k
(48) @ æ2 Ê~ÉË« äD M àÑs Î( \Gñ ÍÒ) z~« ~-ê s äj æ2 ak³ gO ¤ À. 97K õgõ }K ñ } õgÉË Î[14]Ñ2 OYä íQ MÑ äHYís GäGD .g äD zÑ É Gä ós ÉD )éÑ fÆê Ê~É monolith2 Gäók³ ¯Gñ UMK s Í0 ¤ ÇÉ. á õgÑ2 É GäD ÄÑ ñ «6K éfYs gGD .g äD ½gÑ jK quick connectorõ «ÄGñ äDõ 𻪠=Ñ Y ä ßj³z ~-Gñ ä HYís HYK á éßôG2 örs >Wk ³ UMK = à Ê~É monolithõ »s ¤ ÀÉ. 3-2. ÿË @ ·» fÆê à Ê~É monolith z gÆQ §à =õ SEM k³ îûK êõ Fig. 3ê 4Ñ ÷É.
(49) ³ TRMs ÄK Î ä HYí O
(50) . Fig. 2. Representative photos of porous polymeric monolith produced 7 at different monomer contents (a) 50 vol% (b) 5 vol%.. 23. Í z Ñ Âj2 s ÷Ê À2 Fig. 3s Ý
(51) , @ ê monolith2 ¤Qo 1ó ½É Yk³ «P´, à gÆ ³ æ´ À2 as < ¤ À.
(52) Í 30 vol%³ ¬J k³ o Fig. 3(a) ÎÑ2 9GJ à 1ó ½É˳ g ê í h §àgÆõ Í(,
(53) Í 70 vol%³ o Fig. 3(c) ÎÑ2 4? Êo 1ó ½ÉË Yk³ «P´ À2 jÊ K gÆõ ä2 ak³ ÷
(54) . ¶ ä HYí O
(55) . Í ÍG
(56) @ æ2 Ê~É monolithõ g G2 1ó ½ÉQ §à ¿D2 ÝGÊ Æ)« jÊg(2 as < ¤ ÀÉ.. Äê
(57) ÜÍÍ @ æ2 monolith z Ñ Âj2 s ÷Ê À2 Fig. 4õ Ý
(58) , EDMA÷ DVBõ
(59) ³. ÄK ÎÑ2 ço ÆQÑ TRMs
(60) ³ ÄK Î(Fig. 3(b))Ý monolithõ g GÊ À2 1ó ½É ¿DÍ ÊÊ Æ) « jÊK ak³ ÷
(61) . «6K Ëo monolith Y Ñ Äê
(62) Q @ æ2 Ê ~É ½É Äg³ O ¤ À. á õgÑ ÄK TRM, EDMA Ú DVB
(63) 2 𻪠«d!Ñ ¬K ÄgÍ ¿D )éÑ OY ä MÑ2 ä HYí« è³K s ä(O, OY ä« ,}æ´ Ê~ÉÍ @ æ
(64) 𻪠«d!Ñ ¬K Äg 2 Gj ÝGj ê. ¶ ½É Ê~ÉË« ÏI GÊ «Ë« ßG
(65) ³ YGñ monolithõ Gj ê. OY äs 0g ßG2 Ê~É
(66) Ñ ¬K Äg2 𻪠«d!Ñ ¬K ÄgÑ 9Gñ ¬Jk³ ¿³, ä HYí O
(67) Í s ÎÑ2 ßG2 Ê~É ~-Í
(68) Í o ÎÑ 9Gñ ¬Jk³ Ej ³´÷j ê. -Ê ~-Í ³´ÿ ) @ ê ÊÊ Qo õ J¯ 1ó ½ÉË« ³ YGñ jÊK Æ) monolithõ @ Qÿ2 ak³ gê. ä HYí O
(69) Í s ÎÑ2 ßG2 Ê~É ½É ~-Í ¬Jk³ o MdSÑ ³´÷j æÊ, « ³ ¯Gñ §K 1ó ½ÉË« ê. 1ó ½ÉË« ê á Ñ
(70) Ñ g èOê 1ó ½É2 OYäs 0K ßs ( GÊ, 𻪠«d! zÑ OYäo ªê. «³ ¯Gñ Ê~É ½ÉËo ßGÊ ½ÉË « §ào î, à 1ó ½ÉË« 4ê gÆ monolithõ Gj ê. «6K êËo CooperQ Holmes[14] õg êQ Ñ ³j G2 a«.. Fig. 3. SEM images showing the internal structure of porous polymer monoliths produced from TRM in supercritical CO2 at different monomer concentrations (50 oC, 310 bar). (a) 30 vol% (b) 50 vol% (c) 70 vol%. Korean Chem. Eng. Res., Vol. 43, No. 1, February, 2005.
(71) 24. 㧺ö? R. Fig. 5. The effect of monomer concentration on the specific surface area of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. Fig. 4. SEM images showing the internal structure of porous polymer monoliths produced from different monomers in supercritical CO2 (50 vol%, 50 oC, 310 bar). (a) EDMA (b) DVB.. 3-3. §¿L 𻪠«d! Ñ @ æ2 à Ê~É monolith 9 ,
(72) JÑ ?³ s Âj2 ¯É2 ä HYí O
(73) . Q OYä Ft¯ ak³ ÷
(74) .
(75) ¡dÍ @ æ2 Ê~É monolith 9 ,
(76) JÑ Âj2 s ÷Ê À2 Fig. 5õ Ý
(77) , ä HYí O
(78) Í ³_j(TRM Î 40%, EDMA Î 30%) «G ³ ÎÑ2 9,
(79) J« kÎ ÊÊ
(80) s M ç ( :2 as < ¤ À. 6÷ « òÑ2
(81) Í ÍO¤´ @ æ2 monolith 9 ,
(82) J« ¾ ÍG2 as < ¤ À. «6K o
(83) Í ÍO ¤´ ßG2 Ê~É ½É ~-Í (õæ´, Êo 1ó ½É Q §K Dàs Gñ o 9,
(84) Js Í(j æD )é¯ ak³ gê. EDMAÍ TRMÝ 9 ,
(85) J« ¿Ê s çD QÊG2 Í o ao EDMA ÄgÍ TRMÑ 9g ¬Jk³ ¿D )é«¶ _ê.. ¤@¤ C43× C1 2005 2. Fig. 6o OYä Ft ¡dÍ @ æ2 à Ê~É monolith 9 ,
(86) JÑ Âj2 s ÷ a«. Fig. 6s Ý
(87) , OYä Ft« ÍO¤´ @ æ2 Ê~É monolith 9 ,
(88) J« Í G2 as < ¤Í À. «6K ê2 ð»ª Ñ Ft« ÍG
(89) 𻪠KÑ ¬K Ê~É ½É ÄgÍ ÍGÊ, «Ñ ¶ Ê~É ½É ~-Í (õæ´ Êo 1ó ½ÉÍ @ æÊ «Ë« §K Dàs G2) D¯G2 ak³ gO ¤ À. Fig. 5Q Fig. 6 ê³z @ æ2 Ê~É ½É ä HY íÑ ¬K ÄgÍ Ç¤´ §K 1ó ½É³ g ê jÊK Æ) monolithÍ @ ê2 as < ¤ ÀÉ. 3-4. Rockwell 𻪠«d! Ñ @ æ2 Ê~É monolith Rockwell Ñ Âj2
(90) ¡d s Fig. 7Ñ ÷É. Fig. 7 s Ý
(91) ,
(92) Í ÍO¤´ Rockwell Í ÍG2 s ÷Ê À. «2
(93) Í ÍG
(94) @ æ2 monolithÍ Â§K 1ó ½É³ g æ´ Æ)« jÊg(Ê ÊÍ ÍGD )é¯ ak³ gO ¤ À.. Fig. 6. The effect of reaction pressure on the specific surface area of porous polymeric monolith prepared from TRM (50 oC, 310 bar)..
(95) 𻪠«@õ «ÄK à Ê~É Monolith fÆ. OYä Ft« @ æ2 Ê~É monolith Rockwell Ñ Âj2 s ÷Ê À2 Fig. 8s Ý
(96) , 200 bar «G IF Ñ2 OYä Ft« ÍG
(97) Rockwell Í ÍG2 s ÷D2 G(O « Ft p.Ñ2 Ft s M ç( :2 ak³ ÷
(98) . «2 OYä Ft« @ æ 2 Ê~É ÄgÑ s ÂjD2 G(O, ÁêÍ
(99) . Ý ÊD )é¯ ak³ _ê. OYä QÑ« @ æ2 à Ê~É monolith Rockwell Ñ Âj2 s ÷Ê À2 Fig. 9õ Ý
(100) , OYä QÑ « ÍO¤´ Í ÍG2 as < ¤ À. @ æ2 à Ê~É monolith àHJ Ä s ¬Q IJk³, monolith Rockwell õ ³ ¤ À2 örÑ ¬K Y×J õgõ }G. Fig. 7-9b( êÑ »´, MÊ õ »s ¤ À2 ÆQs JÄGÊ, Ýãf³ à
(101) MAA õ ÍGñ MMA ÍÍ @ æ2 Ê~É monolith í Ñ Âj2 s Æ G. OY HYí O M
(102) 2 50 vol%³ Ê_Q ÆQÑ,
(103) ³ TRMOs ÄGñ OY K monolithQ ?
(104) TRMê à
(105) MAA z) 9õ ¡ dQ- fÆK àOY monolith Rockwell ¡dõ Fig. 10. 25. Fig. 9. The effect of reaction time on the Rockwell hardness of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. Fig. 10. The effect of co-polymer content in the reaction mixture on the Rockwell hardness of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. Fig. 7. The effect of monomer concentration on the Rockwell hardness of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. Ñ 9GGñ ÷É. Fig. 10s Ý
(106) , @ æ2 Ê~É monolith Rockwell 2 Íæ2 à
(107) MAA Í 33 vol%Í î )b( ÍG2 as < ¤ ÀÉ. 3-5. ô/ ¬?F @ æ2 Ê~É monolith Äk ¤tÑ Âj2
(108) s ÷Ê À2 Fig. 11s Ý
(109) ,
(110) Í ÍO ¤´ Äk ¤t« ¾ ÝG2 as < ¤ À. « ê
(111) Í ÍO¤´ @ æ2 Ê~É monolith ÊÍ ÍG2) D¯G2 ak³ gê. Äk ¤tÑ Âj2 ñ ÆÊ¡¤Ë o M Ç2 ak ³ ÷
(112) . 4.. Fig. 8. The effect of reaction pressure on the Rockwell hardness of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. û «. àÆJk³ lÄ ÍjÍ o à Ê~É monolithõ fÆG 2 D¬s íèGD .g 𻪠«d! Ñ à Ê~É monolithõ fÆG2 Y×J Æ õ 0Gñ »o ·o {ê ç. Korean Chem. Eng. Res., Vol. 43, No. 1, February, 2005.
(113) 㧺ö? R. 26. Fig. 11. The effect of monomer concentration on the solvent absorption ratio of porous polymeric monolith prepared from TRM (50 oC, 310 bar).. (1) ä HYí O
(114) Í kÎ o Î(10% «G) õ fG
(115) á õgÑ >K HÇ ÆÊ ÆQÑ
(116) Ü ÍÑ îªÇ« äD z =Q ³K + õ à Ê~É monolithõ fÆO ¤ ÀÉ. (2) ä HYí O
(117) Q OYä Ft« ÍG
(118) @ æ2 Ê~É monolith2 Êo 1ó ½É³ g æÊ Æ)« j Êg(2 ak³ ÷
(119) . (3) @ æ2 à Ê~É monolith 9 ,
(120) Jo ä HYí O
(121) Q OYä Ft« ÍO¤´ ÍG2 ak³ ÷
(122) . (4) @ æ2 Ê~É monolith Rockwell 2 ä HYí O
(123) Q OYä QÑ« ÍO¤´ ÍG2 ak³ ÷
(124) . ä HYíÑ Ýãf MAAõ ÍGñ fÆG
(125) monolith Rockwell õ ÍQ ¤ ÀÉ. (5) monolith Äk ¤to
(126) Í ÍO¤´ Ý GÊ, OYä QÑ« ÍO¤´ ÍG2 ak³ ÷
(127) k÷, O Yä Ft o M ÇÉ.. [ ÷ « øéo 2003¸ z ¬HG D ¡ H¬õg9Ñ Gñ õ gæÉ5n.. +S 1. Kiran, E. and Sengers, J. M. H. L., “Supercritical Fluids: Fundamentals for Applications,” Kluwer Academic Publishers, London (1994). 2. McHugh, M. A. and Krukonis, V. J., “Supercritical Fluid Extraction Priciples and Practice,” 2nd ed., Butterworth-Heinemann(1994). 3. Lewandowski, K., Murer, P., Svec, F. and Fréchet, J. M. J., “Highly Selective Chiral Recognition on Polymer Supports, Preparation of a Combinatorial Library of Dihydropyrimidines and its Screening for Novel Chiral HPLC Ligands,” Chem. Commun., 18, 2237-2238 (1998).. ¤@¤ C43× C1 2005 2. 4. Xu, M. C., Brahmachary, E., Janco, M., Ling, F. H., Svec, F. and Fréchet, J. M. J., “Preparation Liquid Chromatographic Separation of Enantiomers by Direct Copolymerizations of Monomers with Single or Twin Chiral Ligands,” J. Chromatogr. A, 928, 2540(2001). 5. Xie, S., Svec, F. and Fréchet, J. M. J., “Rigid Porous PolyacryLamide-Based Monolithic Columns Containing Butyl Methacrylate as a Separation Medium for the Rapid Hydrophobic Interaction Chromatography of Protein,” J. Chromatogr. A, 775, 65-72(1997). 6. Wakayama, H. and Fukushima, Y., “Porous Platinum Fibers Synthesized using Supercritical Fluid,” Chem. Commun., 391-392(1999). 7. Matsuyama, H., “Formation of Porous Flat Membrane by Phase Separation with Supercritical CO2”, J. of Membr. Sci., 194, 157163(2001). 8. Rindfleisch, F., DiNoia, T. P. and McHugh, M. A., “Solubility of Polymers and Copolymers in Supercritical CO2”, J. Phys. Chem., 100, 15581-15587(1996). 9. O’Neill, M. L., Yates, M. Z., Johnson, K. P., Smith, C. D. and Wilkinson, S. P., “Dispersion Polymerization in Supercritical CO2 with a Siloxane-Based Macromonomer: 1. The Particle Growth Regime,” Macromolecules, 31, 2838-2847(1998). 10. O’Neill, M. L., Yates, M. Z., Johnson, K. P., Smith, C. D. and Wilkinson, S. P., “Dispersion Polymerization in Supercritical CO2 with a Siloxane-Based Macromonomer: 2. The Particle Formation Regime,” Macromolecules, 31, 2848-2856(1998). 11. Galia, A., Muratori, A. and Filardo, G., “Dispersion Copolymerization of Vinyl Monomers in Supercritical Carbon Dioxide,” Ind. Eng. Chem., 42(3), 448-455(2003). 12. Cooper, A. I., Hems, W. P. and Holmes, A. B., “Synthesis of Highly Cross-Linked Polymers in Supercritical Carbon Dioxide by Heterogeneous Polymerization,” Macromoleclues, 32, 21562166(1999). 13. Lele, A. K. and Shine, A. D., “Morphology of Polymers Precipitated from a Supercritical Solvent,” AIChE, 38(5), 742-752(1992). 14. Cooper, A. I. and Holmes, A. B., “Synthesis of Molded Monolithic Porous Polymers using Supercritical Carbon Dioxide as the Porogenic Solvent,” Adv. Mater., 11(15), 1270-1274(1999). 15. Cooper, A. I., Wood, C. D. and Holmes, A. B., "Synthesis of Well-Defined Macroporous Polymer Monoliths by Sol-Gel Polymerization in Supercritical CO2”, Ind. Eng. Chem., 39, 47414744(2000). 16. Chatzidoukas, C., Pladis, P. and Kiparissides, C., “Mathematical Modeling of Dispersion Polymerization of Methyl Methacrylate in Supercritical Carbon Dioxide,” Ind. Eng. Chem., 42, 743-751 (2003). 17. Wood, C. D. and Cooper, A. I., “Synthesis of Macroporous Polymer Beads by Suspension Polymerization using Supercritical Carbon Dioxide as a Pressure-Adjustable Porogen,” Macromolecules, 34, 5-8(2001). 18. Tennikov, M. B., Gazdina, N. V., Tennikova, T. B. and Svec, F., “Effect of Porous Structure of Macroporous Polymer Supports on Resolution in High-Performance Membrane Chromatography of Proteins,” J. Chmatogr A, 798, 55-64(1998). 19. Murer, P., Lewandowski, K., Svec, F. and Fréchet, J. M. J., “Onbead Combinatorial Approach to the Design of Chiral Stationary Phases for HPLC,” Anal. Chem, 71, 1278-1284(1999)..
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관련 문서
Abstract − Our study focuses on upgrading real biogas obtained under Indian scenario using carbon capture and uti- lization (CCU) technology to remove carbon dioxide (CO 2 ) and
Abstract − Porous carbon nanofibers(CNF) were synthesized via NaOH activation at 700~900 o C, and the porous CNF-supported PtRu catalysts were evaluated for the anode in direct
Key words: Carbon Dioxide, Immobilized Catalyst, Ionic Liquid, Allyl Glycidyl Ether, Cyclic Carbonate 1.. 그러나 현재까지
and Gupta, R., “The Dry Car- bonate Process: Carbon Dioxide Recovery from Power Plant Flue Gas,” 7th Annual Conference on Carbon Capture & Seques- tration, May,
Abstract − To study the optimal synthesis conditions of aqueous acrylic adhesive using emulsion polymerization, the effects of monomer, surfactant and initiator on the
The experimental results of redox reaction of the synthesized magnetite powder showed that the reduction by hydrogen and the oxidation by carbon dioxide were seldom observed below 400
Abstract − Porous polypropylene membranes were prepared by a thermally induced phase separation method in supercritical CO2, where polypropylene and Camphene were used as
Comparison of mass transfer coefficients of carbon dioxide in gas absorption using the membrane contactor CO2-Water CO2-MEA 20% MEA no plasma no plasmaPlasma treatment