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Modeling the kinetics of essential oil hydrodistillation from juniper berries (Juniperus communis L.) using non-linear regression

机译:使用非线性回归模拟杜松浆果(Juniperus communis L.)精油加氢蒸馏的动力学

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This paper presents kinetics modeling of essential oil hydrodistillation from juniper berries (Juniperus communis L.) by using a non-linear regression methodology. The proposed model has the polynomial-logarithmic form. The initial equation of the proposed non-linear model is q = q∞?(a?(logt)2 + b?logt + c) and by substituting a1=q∞?a, b1 = q∞?b and c1 = q∞?c, the final equation is obtained as q = a1?(logt)2 + b1?logt + c1. In this equation q is the quantity of the obtained oil at time t, while a1, b1 and c1 are parameters to be determined for each sample. From the final equation it can be seen that the key parameter q∞, which presents the maximal oil quantity obtained after infinite time, is already included in parameters a1, b1 and c1. In this way, experimental determination of this parameter is avoided. Using the proposed model with parameters obtained by regression, the values of oil hydrodistillation in time are calculated for each sample and compared to the experimental values. In addition, two kinetic models previously proposed in literature were applied to the same experimental results. The developed model provided better agreements with the experimental values than the two, generally accepted kinetic models of this process. The average values of error measures (RSS, RSE, AIC and MRPD) obtained for our model (0.005; 0.017; –84.33; 1.65) were generally lower than the corresponding values of the other two models (0.025; 0.041; –53.20; 3.89) and (0.0035; 0.015; –86.83; 1.59). Also, parameter estimation for the proposed model was significantly simpler (maximum 2 iterations per sample) using the non-linear regression than that for the existing models (maximum 9 iterations per sample). [Project of the Serbian Ministry of Education, Science and Technological Development, Grant no. TR-35026].
机译:本文介绍了使用非线性回归方法从杜松子(Juniperus communis L.)精油加氢蒸馏的动力学模型。所提出的模型具有多项式-对数形式。提出的非线性模型的初始方程为q =q∞?(a?(logt)2 + b?logt + c)并通过代入a1 =q∞?a,b1 =q∞?b和c1 = q ∞?c,最终方程为q = a1?(logt)2 + b1?logt + c1。在该方程式中,q是在时间t处获得的油量,而a1,b1和c1是要为每个样本确定的参数。从最终方程式中可以看出,表示无穷时间后获得的最大油量的关键参数q∞已经包含在参数a1,b1和c1中。这样,避免了对该参数的实验确定。使用所提出的模型和通过回归获得的参数,可以为每个样品计算出石油加氢精馏的时间值,并将其与实验值进行比较。另外,将先前在文献中提出的两个动力学模型应用于相同的实验结果。与该过程的两个公认的动力学模型相比,开发的模型与实验值具有更好的一致性。从我们的模型获得的误差度量(RSS,RSE,AIC和MRPD)的平均值(0.005; 0.017; –84.33; 1.65)通常低于其他两个模型的相应值(0.025; 0.041; –53.20; 3.89 )和(0.0035; 0.015; –86.83; 1.59)。同样,使用非线性回归对所提出的模型进行参数估计要简单得多(每个样本最多2次迭代),而对现有模型进行参数估计(每个样本最多9次迭代)。 [塞尔维亚教育,科学和技术发展部的项目,赠款TR-35026]。

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