[1] | Ԭ����.�����Ż���ϩԭ�ϵ�����˼��[J].����ʯ��ʯ��,2001,9(10):5-10 | [2] | FOLEY T,GREER D,PUJADO P,et al.Maximizingethylene with MaxEne[J].Hydrocarbon Engineering,2001,6(8):35-41 | [3] | NAPEX Aromatics extraction improves ethylene crackerfeed[J].Hydrocarbon Processing,2005,84(4):29-30 | [4] | WEISSERMEL K,ARPE HJ.Industrial Organic Chem-istry[M].4 ed.Wiley-VCH,Weinheim:2003 | [5] | MEINDERSMA G W,DE HAAN A B.Conceptualprocess design for aromatic/aliphatic separation with i-onic liquids[J].Chemical Engineering Research andDesign.2008,86(7):745-752 | [6] | JONQUIERES A,CLEMENT R,LOCHON P,et al.Industrial state-of-the-art of pervaporation and vapourpermeation in the western countries[J].Journal ofMembrane Science.2002,206(1/2):87-117 | [7] | SMITHA B,SUHANYA D,SRIDHAR S,et al.Sepa-ration of organic-organic mixtures by pervaporation:Are-view[J].Journal of Membrane Science.2004,241(1):1-21 | [8] | ������,�ܴ���,��սʤ,��.����/֬��������������Ĥ���о���չ[J].��ѧ��ҵ�빤��.2009,26(3):262-267 ��� | [9] | YAMAGUCHI T,NAKAO S,KIMURA S.Solubilityand pervaporation properties of the filling-polymerizedmembrane prepared by plasma-graft polymerization forpervaporation of organic-liquid mixtures[J].Industrial&Engineering Chemistry Research.1992,31(8):1- | [10] | ULBRICHTM,SCHWARZ H H.Novel high perform-ance photo-graft composite membranes for separation oforganic liquids by pervaporation[J].Journal of Mem-brane Science.1997,136(1/2):25-33 | [11] | FRAHN J,MALSCH G,MATUSCHEWSKI H,et al.Separation of aromatic/aliphatic hydrocarbons by photo-modified poly(acrylonitrile)membranes[J].Journal ofMembrane Science.2004,234(1/2):55-65 | [12] | [12]����ʯ�ͺͻ�ѧ��ҵ��.SH/T0714-2002,ʯ�����е�������ɲⶨ��[S].����:�й�ʯ��������,2002. |
|