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Estimation of concentration-independent rate-constant (CIRC) for esterification kinetics of biodiesel synthesis from high FFA containing low cost feed stocks

机译:低FFA含有低成本饲料股的生物柴油合成酯化动力学浓度无关率 - 常数(循环)

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The raw material accounts for 60???80% of the total cost of biodiesel fuel produced via transesterification of refined oil. The profitable biodiesel can be produced from low cost feedstocks. But such feed-stocks generally contain large amounts of free fatty acids (FFA). A key challenge is cost-effective pretreatment of high FFA feed-stocks to reduce the FFA below the desired levels prior to the transesterification process. Kinetics of the esterification reaction cannot be computed unless the rate law and values of rate constant are known. Rate constants are determined usually by performing experiments at different reaction conditions. In this work, a novel method is proposed as shown in the Figure 1 for the estimation of rate constants for H2SO4- catalyzed esterification of FFA with methanol for the biodiesel synthesis from the low-cost feedstocks. This method is based on the concept of concentrationindependent rate-constant (CIRC) and equilibrium constant as a function of temperature only. The various steps involved in the method are shown in detail in the figure 2. Techniques of design of experiments (DOE) such as Taguchi method and full-factorial design are used to design the experiments and to perform statistical and regression analysis of the results using software MINITAB 15 to obtain mathematical models for the estimation of rate constants. Effects of catalyst loadings (0.5-2.0 wt %), temperature (40- 60?C), and molar ratio (3-9) on the kinetics are studied. Mathematical models developed for the predictions of kinetics are statistically and kinetically tested through model adequacy check. Models are found to be suitable for kinetics predictions. The CIRCs are then estimated from the predicted kinetics of models. The estimated CIRCs are compared with the experimental values of CIRCs obtained from the validation experiments and most of them are found to be within ?10% deviation.
机译:原料占通过酯交换的精制油生产的生物柴油燃料总成本的60%。盈利的生物柴油可以由低成本原料生产。但这种饲料股通常含有大量的游离脂肪酸(FFA)。关键挑战是高FFA饲料的预处理是在酯交换过程之前将FFA减少到所需水平以下。除非已知速率法和速率常数的速率法,否则不能计算酯化反应的动力学。通常通过在不同反应条件下进行实验来确定速率常数。在这项工作中,提出了一种如图1所示的新方法,用于估计来自低成本原料的生物柴油合成的FFA的H2SO4催化酯化的速率常数估计。该方法基于集中依赖性速率 - 常数(电路)和平衡常数作为温度的概念。该方法涉及的各种步骤在图2中详细示出。实验设计(DOE)的技术,例如Taguchi方法和全因子设计,用于设计实验并执行结果的统计和回归分析软件Minitab 15获得用于估计速率常数的数学模型。研究了催化剂载量(0.5-2.0wt%),温度(40-60℃)和摩尔比(3-9)对动力学的影响。用于预测动力学的数学模型在统计上和动力学通过模型充足的检查进行了动力学测试。发现模型适用于动力学预测。然后从预测的模型动力学估计CICS。将估计的CIRCS与从验证实验中获得的CIRC的实验值进行比较,并且其中大多数被发现在10%的偏差范围内。

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