欢迎登录材料期刊网

材料期刊网

高级检索

超临界流体广泛地应用于能源动力、制冷空调等多个领域,而固体在超临界流体中的溶解度对于工业过程有较大的影响.工程上常用状态方程计算溶解度,本文将结合了重整化群理论的RG-CPA方程推广到了溶解度的计算中,RG-CPA方程能够准确地描述流体在近临界和远临界区域的热力学性质,有效地克服了经典立方型状态方程无法准确描述近临界区域热力学性质的缺点.采用该方法对7种有机固体在超临界CO2中的溶解度进行了计算,并与经典方程进行了比较.结果表明,与经典方程相比,RG-CPA方程能更好地再现极接近临界点处溶解度的陡峭变化规律.

参考文献

[1] Lue L.;Prausnitz JM. .Renormalization-group corrections to an approximate free-energy model for simple fluids near to and far from the critical region[J].The Journal of Chemical Physics,1998(13):5529-5536.
[2] 段黎萍,陆九芳,陈健,李以圭.应用重整化群理论计算超临界水的性质[J].化工学报,2003(01):18-23.
[3] Adam Bymaster;Chris Emborsky;Aleksandra Dominik .Renormalization-Group Corrections to a Perturbed-Chain Statistical Associating Fluid Theory for Pure Fluids Near to and Far from the Critical Region[J].Industrial & Engineering Chemistry Research,2008(16):6264-6274.
[4] 许心皓,段远源.CPA方程结合RG理论计算甲醇、水、氨的性质[J].清华大学学报:自然科学版,2011(05):677-680.
[5] 许心皓,段远源,杨震.RG-CPA方程计算超临界CO2-醇体系汽液相平衡[J].化工学报,2012(05):1331-1337.
[6] Kontogeorgis Georgios M.;Meijer Henk;Hendriks Eric;Moorwood Tony;Yakoumis Iakovos V. .Multicomponent phase equilibrium calculations for water-methanol-alkane mixtures[J].Fluid Phase Equilibria,1999(0):201-209.
[7] M. Sauceau;J. Fages;J.-J. Letourneau;D. Richon .A Novel Apparatus for Accurate Measurements of Solid Solubilities in Supercritical Phases[J].Industrial & Engineering Chemistry Research,2000(12):4609-4614.
[8] Traj Goodarznia;Feridun Esmaeilzadeh .Solubility of an Anthracene, Phenanthrene, and Carbazole Mixture in Supercritical Carbon Dioxide[J].Journal of Chemical and Engineering Data: the ACS Journal for Data,2002(2):333-338.
[9] Hu ZQ.;Yang JC.;Li YG. .Crossover SAFT-BACK equation of state for pure CO2 and H2O[J].Fluid Phase Equilibria,2003(1):25-36.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%