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Yield and kinetic constants estimation in the production of hydroxy fatty acids from oleic acid in a bioreactor by Pseudomonas aeruginosa 42A2

机译:铜绿假单胞菌42A2在生物反应器中由油酸生产羟基脂肪酸的产率和动力学常数估算

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摘要

We modelled the production of hydroxy fatty acids from oleic acid by Pseudomonas aeruginosa 42A2 in a bioreactor with a non-dispersive aeration system. First, we designed an adapted wetted-wall gas-absorption column, offering a k (L)a value of 39.9 h(-1), to enhance oxygen absorption in the culture media and prevent foam formation. Then, we analysed different kinetic models to simulate the yield coefficients and the kinetic constants in this bacterial transformation. Monod model fitting (mu (max1) = 0.51 h(-1), K (S1) = 1.60 C-mol l(-1), mu (max2) = 0.12 h(-1), K (S2) = 0.035 C-mol l(-1), and k (2) = 0.033 h(-1)) showed a good accuracy with the experimental data sets and was chosen for its simplicity. Lastly, mass balances were carried out to establish the stoichiometry of this biotransformation with the following yield coefficients, Iyen (X/OA), Iyen (X/(10S)-HPOME) and Iyen ((10S)-HPOME/(7S10S)-HPOME) of 0.172, 0.347 and 2.388 C-mol C-mol(-1), respectively.
机译:我们模拟了在非分散曝气系统的生物反应器中铜绿假单胞菌42A2由油酸生产羟基脂肪酸的过程。首先,我们设计了一种改良的湿壁气体吸收柱,其k(L)a值为39.9 h(-1),以增强培养基中的氧吸收并防止泡沫的形成。然后,我们分析了不同的动力学模型,以模拟这种细菌转化过程中的产量系数和动力学常数。 Monod模型拟合(mu(max1)= 0.51 h(-1),K(S1)= 1.60 C-mol l(-1),mu(max2)= 0.12 h(-1),K(S2)= 0.035 C -mol l(-1)和k(2)= 0.033 h(-1))在实验数据集上显示出良好的准确性,并且为简单起见对其进行了选择。最后,进行质量平衡以建立该生物转化的化学计量,其屈服系数为Iyen(X / OA),Iyen(X /(10S)-HPOME)和Iyen((10S)-HPOME /(7S10S)- HPOME)分别为0.172、0.347和2.388 C-mol C-mol(-1)。

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