Modelling of multicomponent olefins solubility in polyolefins using Sanchez-Lacombe equation of state

被引:26
作者
Bashir, Muhammad Ahsan [1 ]
Ali, Mohammad Al-haj [2 ]
Kanellopoulos, Vasileios [2 ]
Seppala, Jukka [1 ]
机构
[1] Aalto Univ, Dept Chem & Biotechnol, Espoo 02150, Finland
[2] Borealis Polymers Oy, Borealis Polymers PO PDO, Innotech Proc Technol, Porvoo, Finland
关键词
Sanchez-Lacombe equation of state; Multicomponent solubility; Polyolefins; Crystalinity; Modeling; ASSOCIATING FLUID THEORY; PHASE REACTOR CONDITIONS; LOW-DENSITY POLYETHYLENE; SAFT-VR APPROACH; GAS-PHASE; SEMICRYSTALLINE POLYETHYLENE; DIFFUSION-COEFFICIENTS; 1-HEXENE SORPTION; CARBON-DIOXIDE; ETHYLENE;
D O I
10.1016/j.fluid.2013.08.009
中图分类号
O414.1 [热力学];
学科分类号
摘要
The Sanchez-Lacombe equations of state (SL EoS) was employed to predict the solubility of different alpha-olefins in their corresponding mixtures with polyolefins. Its predictive capabilities depend on binary alpha-olefin/polyolefin interaction parameters, which are extracted from the corresponding binary systems. These parameters can be used directly unless polymer crystallinity is high where fine adjustment is needed. It was found that model predictions were in excellent agreement with the available experimental data for different multicomponent systems over a wide range of pressure, temperature and mixture composition. An accurate quantitative knowledge of olefins solubility in polyolefins is essential for the detailed design and modelling of polymerization reactors. Nevertheless, there are a limited number of studies that deal with modelling of multicomponent alpha-olefins/polyolefin systems. This work can be considered as a part of a comprehensive plant-scale modelling approach for industrial polyolefin manufacturing processes. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:83 / 90
页数:8
相关论文
共 47 条
  • [1] Ethylene and 1-hexene sorption in LLDPE under typical gas phase reactor conditions: A priori simulation and modeling for prediction of experimental observations
    Banasazak, BJ
    Lo, D
    Widya, T
    Ray, WH
    de Pablo, JJ
    Novak, A
    Kosek, J
    [J]. MACROMOLECULES, 2004, 37 (24) : 9139 - 9150
  • [2] Banat Y.A.I., 2006, THESIS U TWENTE NETH, P9
  • [3] Bashir M.A., 2013, INT C REACT ENG POL
  • [4] The Effect of Pure Component Characteristic Parameters on Sanchez-Lacombe Equation-of-State Predictive Capabilities
    Bashir, Muhammad Ahsan
    Ali, Mohammad Al-haj
    Kanellopoulos, Vasileios
    Seppala, Jukka
    Kokko, Esa
    Vijay, Sameer
    [J]. MACROMOLECULAR REACTION ENGINEERING, 2013, 7 (05) : 193 - 204
  • [5] Modeling of the sorption and swelling behavior of semicrystalline polymers in supercritical CO2
    Bonavoglia, B
    Storti, G
    Morbidelli, M
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (03) : 1183 - 1200
  • [6] Modeling polyethylene fractionation using the perturbed-chain statistical associating fluid theory equation of state
    Cheluget, EL
    Bokis, CP
    Wardhaugh, L
    Chen, CC
    Fisher, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (05) : 968 - 988
  • [7] DENSITY-TUNED POLYOLEFIN PHASE-EQUILIBRIA .2. MULTICOMPONENT SOLUTIONS OF ALTERNATING POLY(ETHYLENE PROPYLENE) IN SUBCRITICAL AND SUPERCRITICAL OLEFINS - EXPERIMENT AND SAFT MODEL
    CHEN, SJ
    ECONOMOU, IG
    RADOSZ, M
    [J]. MACROMOLECULES, 1992, 25 (19) : 4987 - 4995
  • [8] Modeling solubilities of subcritical and supercritical fluids in polymers with cubic and non-cubic equations of state
    Chen, Zhen-hua
    Cao, Kun
    Yao, Zhen
    Huang, Zhi-ming
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 2009, 49 (02) : 143 - 153
  • [9] SORPTION OF ORGANIC VAPORS IN POLYETHYLENE
    DOONG, SJ
    HO, WSW
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (06) : 1351 - 1361
  • [10] Evelyne N., 2002, FLUID PHASE EQUILIBR, V203, P133