Modeling of suspension polymerizations in continuous oscillatory baffled reactors (COBR)- Part I: Vinyl acetate polymerization

被引:2
作者
Silva, Jonildo dos Santos [1 ]
Melo, Priamo Albuquerque [1 ]
Marinho, Rita [2 ]
de Jesus, Normando Jose Castro [3 ]
Andrade, Marcio Henrique S. [3 ]
Pinto, Jose Carlos [1 ]
机构
[1] Univ Fed Rio de Janeiro, Programa Engn Quim, COPPE, Cidade Univ, BR-21941972 Rio De Janeiro, RJ, Brazil
[2] Braskem SA, Polo Petroquim Camacari, Rua Hidrogenio,3342, BR-42810280 Camacari, BA, Brazil
[3] Braskem SA, Campos Eliseos,Rua Marumbi,1400, BR-25221000 Duque De Caxias, RJ, Brazil
关键词
Suspension; Polymerization; COBR; Vinyl acetate; Modeling; RESIDENCE TIME DISTRIBUTION; HEAT-TRANSFER; THERMAL-CONDUCTIVITY; SIZE DISTRIBUTION; DROPLET SIZE; SCALE-UP; FLOW; LIQUID; BATCH; DISPERSION;
D O I
10.1016/j.ces.2024.119845
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, a phenomenological model to represent suspension polymerizations in a continuous oscillatory baffled reactor is presented for the first time. The reactor is described as a series of tanks of equal volume connected. Additionally, a backflow stream is also included to simulate a backmixing mechanism. The proposed model considers mass, energy, statistical moments balances and regulatory control loops. Furthermore, the heat transfer coefficient is modeled as a function of the oscillatory conditions and the properties of the suspension. The model predictions are compared with available experimental data and good agreement is observed. The effects of key model parameters on model responses are also investigated. It is shown that initiator type and injection points must be carefully planned to avoid excessive temperature gradients along the reactor length. Given the thorough description of kinetic and heat transfer phenomena, the model can be used for reactor design and process scale up.
引用
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页数:17
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