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Termodinamica Continua Revisao Bibliografica Final

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Revisão bibliográfica que cita os principais artigos na área da Termodinâmica Contínua .
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   Artigos científicos sobre aplicação da Termodinâmica Contínuana Engenharia Química e na Engenharia de Petróleo comenfoque no Equilíbrio de ases Os problemas práticos relacionados com as misturas complexas (petróleo e suas frações) têm natécnica dos pseudo-componentes um grande aliado. Mas essa técnica apresenta limitações. Outromodo de atacar a uest!o é usando-se um camin o alternati#o c amado de $%ermodin&mica'ontnua. *lguns dos artigos mais rele#antes est!o citados a seguir. O estudo desses artigos proporcionará aos interessados um meio de entrar em contato com essa técnica.+e len, . /0t1sc , M. %. 'ontinuous t ermod2namics of multicomponent mixtures, in 34roceedings of 5 t  6nternational 'onference on % ermod2namics, Merseburg (78/), pages 9:;<:,:=>?./0t1sc , M. %. +e len, . 'ontinuous t ermod2namics of complex-mixtures, @luid 4 aseAuilibria, :93 BB<-BC9, Oct, :=>Ca.+e len, . /0t1sc , M. %. *pplication of continuous t ermod2namics to t e liuid-#apor-euilibrium and distillation, ' emisc e %ec niD, C< (:?)3 <C9-<C<, :=>Cb.+e len, . /0t1sc , M. %. Eeparate treatment of paraffins and aromatics in complex 2drocarbonmixtures b2 continuous t ermod2namics, Feitsc rift @ur 4 2siDalisc e ' emie-Geip1ig, B5< (5)3:?9=-:?5?, :=>9.+e len, . /0t1sc , M. %. Hergmann, I. 4 ase rule in continuous t ermod2namics, Feitsc rift @ur 4 2siDalisc e ' emie-Geip1ig, B5< (:)3 :=:-:=9, :=>9.'otterman, /. G. 8imitrelis, 8. 4rausnit1, I. M. Eupercritical-fluid extraction calculations for  ig -boiling petroleum fractions using propane ; *pplication of continuous t ermod2namics, >>(=)3 J=5->?:, :=>9. Heric te 8er Hunsen-7esellsc aft-4 2sical ' emistr2 ' emical 4 2sics, >>(=)3 J=5->?:, :=>9./0t1sc , M. %. +e len, . Auilibrium flas #apori1ation cur#es b2 continuous t ermod2namics,Feitsc rift @ur 4 2siDalisc e ' emie-Geip1ig, B55 (B)3 CB=-CC=, :=><.Hergmann, I. +e len, . /0t1sc , M. %. Etabilit2 studies Kit t e aid of continuoust ermod2namics, Feitsc rift @ur *ngeKandte Mat ematiD Lnd Mec aniD, 5< (>)3 C9C-C<C, :=><.'otterman, /. G. Hender, /. 4rausnit1, I. M. 4 ase-euilibria for mixtures containing #er2 man2components ; 8e#elopment and application of continuous t ermod2namics for c emical processdesign, 6ndustrial  Angineering ' emistr2 4rocess 8esign and 8e#elopment, B9 (:)3 :=9-B?C,:=><.'otterman, /. G. 4rausnit1, I. M. @las 'alculations for 'ontinuous or Eemicontinuous MixturesLsing an Auation of Etate, 6ndustrial  Angineering ' emistr2 4rocess 8esign and 8e#elopment,B9 (B)3 9C9-99C, :=><.+e len, . /0t1sc , M. %. Hergmann, I. 'ontinuous t ermod2namics of multicomponent s2stems,*6' A Iournal, C: (J)3 ::C5-::9>, :=><.7utsc e, H. 4 ase-euilibria in oleoc emical industr2 ; *pplication of continuous t ermod2namics,@luid 4 ase Auilibria, C?3 5<-JC, O'% :=>5.Nillman, H.%. %ea, *. E. 'ontinuous t ermod2namics of p ase-euilibria using a multi#ariatedistribution function and an euation of state, *6' A Iournal, CB (:B)3 B?5J-B?J>, :=>5.  /0t1sc , M. %. +e len, . Haumann, @. *pplication of continuous t ermod2namics to t e #apor-liuid-euilibrium of complex 2drocarbon mixtures, Feitsc rift @ur 4 2siDalisc e ' emie-Geip1ig, B5> (C)3 5:9-5:>, :=>J.+e len, . /0t1sc , M. %. 'omplex multicomponent distillation calculations b2 continuoust ermod2namics, ' emical Angineering Ecience, 9B (B)3 BB:-BCB, :=>J.Nang, E. . N iting, N. H. * group-contribution, continuous-t ermod2namics frameKorD for calculation of #apor-liuid-euilibria, 'anadian Iournal of ' emical Angineering, 5< (9)3 5<:-55:,:=>J.+e len, . /0t1sc , M. %. /u1icDa, P. EadoKsDi, 7. 'ontinuous t ermod2namics of t e liuid-liuid euilibrium for s2stems containing petroleum fractions, Feitsc rift @ur 4 2siDalisc e' emie-Geip1ig, B5= (<)3 =?>-=:5, :=>>./0t1sc , M. %. +e len, . Ec umann, I. @las calculations for a crude-oil b2 continuoust ermod2namics, ' emical Angineering 'ommunications, J:3 ::C-:B<, :=>>./0t1sc , M. %. 'ontinuous % ermod2namics, 4ure and *pplied ' emistr2, 5: (5)3 ::?<-:::9, :=>=./0t1sc , M. %. +e len, . Ec umann, I. 'omputer-simulation of complex multicomponent 2drocarbon distillation b2 continuous t ermod2namics, @luid 4 ase Auilibria, <:3 :CC-:95, :=>=.Qing, R. 7. Qe, /. S. u, Q. 4 ase-euilibria for complex-mixtures ; 'ontinuous-t ermod2namics met od based on spline fit, @luid 4 ase Auilibria, <C3 9?J-9:9, :=>=.Massanet1, I. /0t1sc , M. %. +e len, . Hubble and deK-point calculations b2 continuoust ermod2namics using a fourier-series, Feitsc rift @ur 4 2siDalisc e ' emie-Geip1ig, BJ: (C)3 99C-9<?, :==?.'otterman, /. G. 4rausnit1, I. M. *pplication of continuous t ermod2namics to natural-gasmixtures, /e#ue de GT6nstitut @rancais du 4etrole, 9< (<)3 5CC-59C, :==?.'otterman, /. G. 'ontinuous t ermod2namics for p ase-euilibrium calculations in c emical process design, *bstracts of 4apers of % e *merican ' emical Eociet2, B?:3 CJ-6A' 4arte3 :, *4/ :9, :==:.a2nes, . N. Matt eKs, M. *. 'ontinuous-mixture #apor-liuid-euilibria computations based ontrue boiling-point distillations, 6ndustrial  Angineering ' emistr2 /esearc , C? (>)3 :=::-:=:<,:==:.' eluget, A. G. Pera, I. . 4 ase-euilibria calculations for ill-defined mixtures using t e 4/EPeuation of state, 'anadian Iournal of ' emical Angineering, 5= (5)3 :CJ9-:C>:, :==:.Gira-7aleana, '. 4once-/amire1, G. 7arcia-Eanc e1, @. * molecular t ermod2namic approac tot e prediction of p ase-euilibria in reser#oir simulation, 'anadian Iournal of ' emicalAngineering, J? (C)3 <<=-<5>, :==B.Qoo, E. I. Gee, E. Q. Qoo, +. 4. 4 ase-euilibria of ea#2 raK p2rol2sis gasoline continuousmixture using 4eng-/obinson euation of state, +orean Iournal of ' emical Angineering, = (B)3 >=-=J, :==B.*ngelos, '. 4. H agKat, E. P. Matt eKs, M. *. Measurement and modeling of p ase-euilibriaKit s2nt etic multicomponent mixtures, @luid 4 ase Auilibria, JB3 :>=-B?=, :==B.ennig, /. 7umprec t, *. Suit1sc , +. 6n#estigations of t e separation of multicomponentmixtures on t e example of t e lube oil distillation plant Feit1, ' emisc e %ec niD, 99 (B)3 C=-99,:==B.Pasue1, *. Hriano, I. 7. % ermal-conducti#it2 of 2drocarbon mixtures ; * perturbationapproac , 6ndustrial  Angineering ' emistr2 /esearc , CB (:)3 :=9-:==, :==C.  +oDal, E. G. Ea2eg , E. 7. 7eorge, *. A. 4 ase-euilibria of crude oils using t e continuoust ermod2namics approac , 'anadian Iournal of ' emical Angineering, J: (:)3 :C?-:9?, :==C.4arD, I. +im, . 'ontinuous t ermod2namics of p ase-euilibria using t e beta-distributionfunction and an euation of state, +orean Iournal of ' emical Angineering, :? (B)3 J:-JJ, :==C.+ramar1, I. N2c1esan2, *. 8e#elopment and application of continuous t ermod2namics for complex c emical-euilibria calculations, ' emical Angineering Ecience, 9> (=)3 :55<-:5JC, :==C.Erini#asan, G. +abadi, P. U. % ermod2namics of coal-deri#ed fluids .B. #apor-liuid-euilibria of coal liuid fractions, @uel, JC(<)3 J:9-JBB, :==9.+e len, . HroKar1iD, 8. 'ontinuous t ermod2namics ; *n approac to t e treatment of complexmulticomponent s2stems, ' emie 6ngenieur %ec niD, 55 (:?)3 :C95-:C<?, :==9.Giragaleana, '. @iroo1abadi, *. 4rausnit1, I. M. 'omputation of compositional grading in 2drocarbon reser#oirs ; *pplication of continuous t ermod2namics, @luid 4 ase Auilibria, :?B(B)3 :9C-:<>, :==9.7eana, 8. @eroiu, P. 'alculation of PGA for semicontinuous mixtures b2 a general cubic euationof state, /e#ue /oumaine de ' imie, C= (::)3 :CJ<-:C>J, :==9.%amim, I. allett, N. G. . * continuous t ermod2namics model for multicomponent droplet#apori1ation, ' emical Angineering Ecience, <? (:>)3 B=CC-B=9B, :==<.Matt eKs, M. *. Gi, @. %oKler, H. @. Hell, 8.*. Papor-liuid-euilibrium measurements Kit semicontinuous mixtures, @luid 4 ase Auilibria, ::: (:)3 :?:-:::, :==<.F ang, '. . Gi, '. G. @ang, R. '. % ree p ase flas calculation under ig pressure usingcontinuous t ermod2namics met od, C rd  6nternational E2mposium on ig 4ressure ' emicalAngineering, A%, Furic , EKit1erland, 6nst. 4roc. Angn.  'r2ogen, O'% ?J-?=, :==5, #on/o r,4. /. e %repp, '. (editors), in 3 ig 4ressure ' emical Angineering, Eérie de li#ros3 4rocess%ec nolog2 4roceedings, Polume3 :B3 99:-999, :==5.Suiroga, M. A. 'ampanella, A. *. 'omparison of met ods for c aracteri1ation of complexmixtures, ' emical Angineering  %ec nolog2, := (B)3 :?C-::B, :==5.#on Nat1dorf, /. Maruardt, N. @ull2 adapti#e model si1e reduction for multicomponentseparation problems, Ioint 5 t  6nternational E2mposium on 4rocess E2stems AngineeringVC? t Auropean E2mposium on 'omputer *ided 4rocess Angineering (4EA =J-AE'*4A-J), %rond eim, UorKa2, Ma2 B<-B=, :==J. 'omputers  ' emical Angineering, B: (E)3 E>::-E>:5, :==J.Giu, I. G. Nong, 8. E. . /igorous implementation of continuous t ermod2namics usingort onormal pol2nomials, @luid 4 ase Auilibria, :B= (:-B)3 ::C-:BJ, :==J.Ge/o2, E. He ar, A. Lngerer, 4. Papour-liuid euilibrium data for s2nt etic 2drocarbonmixtures. *pplication to modelling of migration from source to reser#oir rocDs, @luid 4 aseAuilibria, :C< (:)3 5C->B, :==J./oc oc1, 7. G. 'astier, M. Eandler, E. 6. 'ritical point calculations for semi-continuous mixtures,*6' A :==J Epring Meeting, ouston, %exas, *6' A, Mar ?=-:C, :==J. @luid 4 ase Auilibria,:C= (:-B)3 :CJ-:<C, :==J.Manafi, . Mansoori, 7. *. 7 otbi, E. 4 ase be a#ior prediction of petroleum fluids Kit minimum c aracteri1ation data, Iournal of 4etroleum Ecience and Angineering, BB (:-C)3 5J-=C,:===.allett, N. G. . * simple model for t e #apori1ation of droplets Kit large numbers of components, 'ombustion and @lame, :B: (:-B)3 CC9-C99, B???PaDili-Ue1 aad, 7. /. Modarress, . Mansoori, 7. *. 'ontinuous t ermod2namics of petroleumfluids fractions, 9?(<)3 9C:-9C<, ' emical Angineering and 4rocessing, B??:.  HroKar1iD, 8. Matt ai, M. Modelling of t e sol#ent-deoiling process of Kaxes b2 continuoust ermod2namics, 4etroleum Ecience and %ec nolog2, B? (=-:?)3 :::=-::9?, B??B.F u, 7. E. /eit1, /. 8. * model for ig -pressure #apori1ation of droplets of complex liuidmixtures using continuous t ermod2namics, 9< (C)3 9=<-<?J, B??B.@ang, N. I. Gei, S. @. 'ontinuous t ermod2namic correlation and calculation of #apor pressure and#apor-liuid euilibrium constant of 2drocarbon fuel fractions, @luid 4 ase Auilibria, B:C (:-B)3:B<-:C>, B??C.HroKar1iD, 8. 4 ase-euilibrium calculations for n-alDane plus alDanol s2stems using continuoust ermod2namics, :J t  6nternational 'onference for ' emical % ermod2namics, /ostocD, 7erman2,ILG B>-*L7 ?B, B??B, 6nt *ssoc ' em % ermod2nam 6L4*', @luid 4 ase Auilibria, B:J (B E6)3:B<-:C<, B??9.Iacome, 4. *. 8. 4eixoto, @. '. 4latt, 7. M. * ón, P. /. /. * neK approac to distillation of continuous mixtures3 Modelling and simulation, Gatin *merican *pplied /esearc , C< (C)3 BCC-BC=,B??<.8atta, *. +. Eing , E. /. 'onsider continuous t ermod2namics approac for modeling,2drocarbon 4rocessing, >5 (:)3 J=-><, B??J.HroKar1iD, 8. 'ontinuous t ermod2namics of binar2 associating s2stems, @luid 4 ase Auilibria,B<9 (:-B)3 :J9-:>J, B??J.Mansoori, 7. *. * unified perspecti#e on t e p ase be a#iour of petroleum fluids, 6nternationalIournal of Oil 7as and 'oal %ec nolog2, B (B)3 :9:-:5J, B??=. Uasrolla i, @. /oodpe2ma, E . PaDili-Ue1 aad, 7. /. Giuid-liuid euilibrium calculations for met anol-gasoline blends using continuous t ermod2namics, @luid 4 ase Auilibria, B>9 (:)3 :-=,B??=.%ian, G. Nang, I. E en, H. Giu, I. % e Modeling of /esidue Eol#ent 8easp alting 4roductMolecular Neig t 8istribution Kit 'ontinuous % ermod2namics, 4etroleum Ecience and%ec nolog2, B> (:9)3 :955-:9J<, B?:?.allett, N. G. . Gegault, U. P. Modelling biodiesel droplet e#aporation using continuoust ermod2namics, @uel, =? (C)3 :BB:-:BB>, B?::.' eng, N. G. E en, '. Gee, '.-f. @. *pplication of continuous t ermod2namics met od to fueldroplet e#aporation, *EMA 6nternal 'ombustion Angine 8i#ision @all %ec nical 'onference,Nestport 6nno#at 6nc, Pancou#er, 'anada, EA4 BC-B5, B?:B, *EMA, 6nternal 'ombus. Angine 8i#.,4roceedings of % e *EMA 6nternal 'ombustion Angine 8i#ision @all %ec nical 'onference, B?:B3>C:->C>, B?:B/odrigues, /. '. * on, P. /. /. Gage, 4. G. '. *n adapti#e c aracteri1ation sc eme for t esimulation of multistage separation of continuous mixtures using t e uadrature met od of moments, @luid 4 ase Auilibria, C:>3 :-:B, B?:B.Aspada, I. I. @ernande1, E. Pelasco, G. 'oto H. A#aluation of different met odologies todetermine t e n-paraffin distribution of petroleum fractions, @uel, :?=3 9J?-9J<, B?:C.4etitfrere, M. Uic ita, 8. P. Montel, @. Multip ase euilibrium calculations using t e semi-continuous t ermod2namics of 2drocarbon mixtures, @luid 4 ase Auilibria, C5B3 C5<-CJ>, B?:9.Mans ad, *. +. Mans ad, M. +. /ostami, . Mode , E. M. Pag efi, M. % e associationt ermod2namics modeling of asp altene precipitation, 4etroleum Ecience and %ec nolog2, CB (:)3<:-5?, B?:9.
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