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Numerical modeling of chemical recovery from black liquor char.

机译:从黑液炭中化学回收的数值模拟。

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A complete CFD model for the char burning stage of chemical recovery from black liquor is presented. Chemical recovery from black liquor is characterized by the occurrence of multiple, simultaneous reactions occurring in dynamic flow conditions. Rate equations for the different chemical reactions are incorporated into a multiphase CFD code MFIX. Rate equations for sulfate reduction by carbon, gasification of carbon by CO2 and H2O, and, COS and H2S formation, are incorporated into MFIX, to simulate the chemical kinetics occurring in the char burning stage. Oxidation of carbon and Na 2S by O2 are also included.;Pyrolysis of black liquor char in the presence of N2, gasification in the presence of CO2 and H2O were simulated. Results for pyrolysis and gasification, and variation with respect to temperature are presented. Two different models for sulfate reduction are compared with each other and with published experimental results. Competitive consumption of carbon by sodium sulfate and gasification reactions is studied and the effects of temperature, and heating rates of solids are discussed.
机译:提出了用于从黑液中回收化学物的焦炭燃烧阶段的完整CFD模型。从黑液中回收化学药品的特征是在动态流动条件下发生多个同时发生的反应。将不同化学反应的速率方程式合并到多相CFD代码MFIX中。 MFIX结合了碳的硫酸盐还原速率,碳的二氧化碳和H2O气化以及COS和H2S形成的速率方程,以模拟在炭燃烧阶段发生的化学动力学。还包括O2对碳和Na 2S的氧化。模拟了在N2存在下黑液炭的热解,在CO2和H2O存在下的气化。给出了热解和气化的结果,以及温度的变化。将两种不同的硫酸盐还原模型进行了比较,并与已发表的实验结果进行了比较。研究了硫酸钠和气化反应的竞争性碳消耗,并讨论了温度和固体加热速率的影响。

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