Development of Volterra-Hybrid and Laguerre models for phenolic resin formation, resol-type, in batch reactors

C. Medina-Ramos, J. Betetta-Gomez, D. Carbonel-Olazabal, M. Pilco-Barrenechea
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引用次数: 2

Abstract

The phenolic resin formation process it can improve if phenol-formaldehyde reaction can be expressed by novel models in which its exothermicity, as well as its chemistry kinetics, is involve. For obtain such objective, the identification process is performed by using the formalisms, Volterra-Hybrid (VL) and Laguerre (LM), as proposed. Nevertheless, is noteworthy that this work is focused in identification the behavior of this reaction in resol-type resin synthesis, under conditions of molar excess and alkaline conditions in industrial batch reactors. In this study, all behavior patterns of the process are mathematically described. The process is started up by heating the reactants, up to reach 62°C in which is reached the activation energy, whereby is must stop the heating action due to manifesting exothermicity of the reaction. Then with this temperature within the reactor, the second stage starts up by applying water in the cooling jacket for smoothing the exothermicity degree, and minimize the risk at the system, in this stage the reactants should reach 102°C. Then the third phase is started up, such that the steam that not yet is part of the resin, it refluxes between a heat exchanger and the reactor. The goal of this activity is reach to compensate the exothermicity. Nevertheless this reflux action has an average duration of 45 min, and when reactor is cooled 101°C only the phenolic resin should be keep inside reactor, thereby the remainder of water must be excluded. Finally, around 100°C start the fourth phase, it which finishes when the reactor is cooling at the temperature of 50°C, and then all process is closed by adding around 1.5% of ethanol. The methodology applied has shown an acceptable fitting between model and data, which it means the model, presents important prospects as a tool to automate the exothermic batch reactors with strong challenges by using mathematical models, without the complexity of the chemical equations.
间歇反应器中酚醛树脂形成的Volterra-Hybrid和Laguerre模型的发展
如果苯酚-甲醛反应可以用涉及其放热性和化学动力学的新模型来表达,则可以改善酚醛树脂的形成过程。为了实现这一目标,识别过程是通过使用Volterra-Hybrid (VL)和Laguerre (LM)的形式进行的。然而,值得注意的是,这项工作的重点是在工业批式反应器中,在摩尔过量和碱性条件下,鉴定该反应在溶解型树脂合成中的行为。在这项研究中,所有的行为模式的过程是数学描述。该过程通过加热反应物开始,加热到62℃,达到活化能,由于反应的放热性,必须停止加热作用。然后在反应堆内的这个温度下,第二阶段启动,在冷却套中加水以平滑放热度,并最小化系统的风险,在这个阶段反应物应该达到102°C。然后第三阶段开始,这样的蒸汽,还不是树脂的一部分,它在热交换器和反应器之间回流。这种活动的目的是达到补偿放热。然而,这种回流作用的平均持续时间为45分钟,当反应器冷却到101°C时,只有酚醛树脂应保留在反应器内,因此必须排除剩余的水。最后,在100°C左右开始第四阶段,当反应器在50°C温度下冷却时结束,然后通过添加约1.5%的乙醇关闭所有过程。所采用的方法表明,模型和数据之间的拟合是可以接受的,这意味着该模型具有重要的前景,可以作为一种工具,通过使用数学模型来自动化具有强大挑战的放热间歇反应器,而不需要化学方程的复杂性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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