[1] 张国锋. 焦化重油精制[D]. 北京:北京化工大学, 2010 Zhang Guofeng. Purification of coking heavy oil[D]. Beijing:Beijing University of Chemical Technology, 2010(in Chinese)
[2] Brzozowska T, Zielinski J, Machnikowski J. Effect of polymeric additives to coal tar pitch on carbonization behaviour and optical texture of resultant cokes[J]. Journal of Analytical and Applied Pyrolysis, 1998, 48(1):45-58
[3] Buckland B C, Drew S W, Connors N C, et al.Microbial conversion of indene to indandiol:A key intermediate in the synthesis of CRIXIVAN[J]. Metabolic Engineering, 1999, 1(1):63-74
[4] Lu M, Mulholland J A. Aromatic hydrocarbon growth from indene[J]. Chemosphere, 2001, 42(5):625-633
[5] Hiroaki M, Youko S. Production process of indene:US, 6818121[P]. 2004-11-16
[6] Wilson G M. Vapor-Liquid equilibrium. X I. A new expression for the excess free energy of mixing[J]. Journal of the American Chemical Society, 1964, 86(2):127-130
[7] Renon H, Prausnitz J M. Local compositions in thermodynamic excess functions for liquid mixtures[J]. AIChE Journal, 1968, 14(1):135-144
[8] Abrams D S, Prausnitz J M. Statistical thermodynamics of liquid mixtures:A new expression for the excess Gibbs energy of partly or completely miscible systems[J]. AIChE Journal, 1975, 21(1):116-128
[9] Herington E F G. Tests for the consistency of experimental isobaric vapor-liquid equilibrium data[J]. J Inst Petrol, 1951, 37:457-470
[10] 程能林. 溶剂手册[M]. 第4版. 北京:化学工业出版社, 2008
[11] David R L. CRC handbook of chemistry and physics[M]. 87th ed. Taylor and Francis:Boca Raton, FL, 2007
[12] Horstmann S, Gardeler H, Bölts R, et al. Vapor-Liquid equilibria and excess enthalpy data for the binary systems benzene+benzonitrile and toluene+ benzonitrile covering the temperature range from 323.15 to 413.15 K[J]. Journal of Chemical & Engineering Data, 1999, 44(3):539-543
[13] Poling B E, Prausnitz J M, John P O C, et al. The properties of gases and liquids[M]. New York:McGraw-Hill, 2001
[14] 马沛生, 李永红. 化工热力学[M]. 第2版. 北京:化学工业出版社, 2010
[15] Mohsen-Nia M, Memarzadeh M R. Isobaric (vapour+ liquid) equilibria for the (1-propanol+1-butanol) binary mixture at (53.3 and 91.3) kPa[J]. The Journal of Chemical Thermodynamics, 2010, 42(6):792-796
[16] Wisniak J. The Herington test for thermodynamic consistency[J]. Industrial & Engineering Chemistry Research, 1994, 33(1):177-180
[17] 高光华. 化工热力学[M]. 第2版. 北京:清华大学出版社,2000
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