کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
687178 889302 2011 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Estimation of equilibrium parameters using differential evolution in reactive extraction of propionic acid by tri-n-butyl phosphate
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تکنولوژی و شیمی فرآیندی
پیش نمایش صفحه اول مقاله
Estimation of equilibrium parameters using differential evolution in reactive extraction of propionic acid by tri-n-butyl phosphate
چکیده انگلیسی

The graphical and conventional optimization methods, used for the estimation of equilibrium parameters, do not guarantee the global optimum values. In this study, the equilibrium parameters are estimated using a well proven evolutionary based optimization routine [differential evolution (DE)]. For the estimation of stoichiometry and equilibrium constants, experiments are carried out for the reactive extraction of propionic acid using tri-n-butyl phosphate (TBP) dissolved in n-decane (inert diluent) and 1-decanol (modifier). The number of TBP molecules (n) in the acid:TBP complex and equilibrium extraction constant (KE) using 1:1 volume ratio of 1-decanol and n-decane as a diluent, are determined through proposed mathematical model using graphical methods as well as the differential evolution algorithm (DE, an optimization routine) and found that the predicted values of distribution coefficient (KD) using DE are closely matching with the experimental values of KD. 1:1 complexes between TBP and acid are formed in most of the cases. The enthalpy and entropy of reactive extraction of propionic acid using TBP are also determined and found to be −12.47 kJ mol−1 and −32.42 J mol−1 K−1, respectively. The results of present study will be useful to intensify the recovery of propionic acid from fermentation broth (bio-separation) and aqueous waste stream.


► The reactive extraction of propionic acid using tri-n-butylphosphate dissolved in n-decane and 1-decanol carried out.
► The graphical and differential evolution (DE) methods are employed for the estimation of equilibrium parameters.
► The effect of various parameters such as modifier, extractant and acid concentrations, and temperature on the extractability is determined.
► The enthalpy and entropy of reaction are estimated.
► The predicted values of distribution coefficient (KD) using DE are closely matching with the experimental values of KD.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 50, Issue 7, July 2011, Pages 614–622
نویسندگان
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