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UNIFAC模型预测含α-蒎烯体系的汽液平衡数据 被引量:3

Prediction of VLE data for system containing α-pinene by UNIFAC model
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摘要 α-蒎烯具有一个特殊的双环双键结构。为更准确地预测含α-蒎烯体系的汽液平衡数据,利用UNIFAC模型原理对α-蒎烯进行基团重新划分,可得到一个大基团双环[3.1.1]-2-庚烯基与3个CH3。通过对含α-蒎烯二元汽液平衡数据进行拟合,得到新基团双环[3.1.1]-2-庚烯基与CH3、C C、ACH、ACCH3基团间的相互作用参数,扩大了UNIFAC模型的应用范围。与原始UNIFAC模型仅利用CH3、C C、ACH、ACCH3基团预测出的含α-蒎烯三元体系汽液平衡数据进行比较,新基团模型预测的气相组成平均偏差以及温度平均偏差比原始基团模型的偏差要更小,说明新基团的划分更为合理。 a-Pinene has a special bicyclo and C=C structure. In order to predict the vapor-liquid equilibrium (VLE) data for the system containing a-pinene more accurately, a-pinene was divided into one bicyclo[3.1.1 ]hept-2-ene and three CH3 according to the theory of UNIFAC model. With the correlation of VLE data for the binary system containing a-pinene, group interaction parameters for bicyclo[3.1.1]hept-2-ene with CH3, C=C, ACH and ACCH3 were obtained, which expands the application of the UNIFAC model. Comparing with the original UNIFAC model using only CH3, C=C, ACH and ACCH3 to predict VLE data of ternary system containing a-pinene, the average deviation of vapor composition and temperature from the prediction of VLE data by new group parameters are smaller than that by the original group parameters, indicating that the new group for a-pinene is more reasonable.
出处 《化工学报》 EI CAS CSCD 北大核心 2014年第9期3309-3316,共8页 CIESC Journal
基金 广西石化资源加工及过程强化技术重点实验室主任基金资助项目(2012Z01) 广西硕士研究生科研创新项目(YCSZ2012004)~~
关键词 汽液平衡 活度系数 模型 基团贡献法 预测 a-蒎烯 vapor-liquid equilibrium activity coefficient model group contribution method prediction a-pinene
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  • 1张高博,樊栓狮,华贲,郎雪梅,余金森.适用于分馏塔改造的回流比优化方法[J].化工进展,2011,30(S1):787-792. 被引量:1
  • 2刘保柱.利用PRO/Ⅱ和Excel求解精馏塔最优回流比[J].计算机与应用化学,2006,23(11):1150-1152. 被引量:11
  • 3廖丹葵,孟学林,武向红,陈小鹏,郑丹星,童张法.α-蒎烯+对伞花烃和β-蒎烯+对伞花烃二元体系超额焓的测定[J].物理化学学报,2006,22(11):1419-1422. 被引量:4
  • 4Liao D K, Meng X L, Tong Z F, et al. Excess molar enthalpies of α-pinene + β-pinene + p-cymene at (298.15, 308.15 and 319.15) K and at atmospheric pressure [J]. J Chem Eng Data, 2007, 52(3): 808-811.
  • 5Bemado-Gil M G, Ribeiro M A. Vapour-liquid equilibrium of binary systems based on pine resin [J]. Fluid Phase Equilibria, 1989 (53): 15-22.
  • 6Bemado-Gil M G, Barreiros A. Vapour-liquid equilibrium of α-pinene + β-pinene at 53.3 and 80 kPa [J]. Fluid Phase Equilibria, 1994(100): 283-291.
  • 7Nadais M H, Bemado-Gil M G. Vapour-liquid equilibrium of α-pinene + limonene at reduced pressures [J]. Fluid Phase Equilibria 1993, 91(2): 321-330.
  • 8Rodrigues M F, Bemado-Gil M G. Vapor-liquid equilibrium of binary mixtures of limonene with a-pinene and β-pinene at reduced pressures [J]. J Chem Eng Data, 1995, 40(6): 1193-1195.
  • 9Rodrigues M F, Bemardo-Gil M G. Vapor-liquid equilibrium data of α-pinene + β-pinene + limonene at 80 kPa and 101 kPa [J]. J Chem Eng Data, 1996, 41(6): 581-585.
  • 10Bemado-Gil M G, Ribeiro M A. Vapor-liquid equilibrium of binary mixtures of β-pinene with limonene and p-cymene at atmospheric pressure [J]. Fluid phase equilibria, 1993(85): 153-160.

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