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Optimal reaction conditions for pyridine synthesis in riser reactor 被引量:3
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作者 Shuaishuai Zhou Zelong Liu +4 位作者 Xiao Yan Qin Di Mengxi Liu Chunxi Lu guangzhou jin 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2018年第7期1499-1507,共9页
Pyridine has been generally synthesized by aldehydes and ammonia in a turbulent fluidized-bed reactor. In this paper, a novel riser reactor was proposed for pyridine synthesis. Experiment result showed that the yield ... Pyridine has been generally synthesized by aldehydes and ammonia in a turbulent fluidized-bed reactor. In this paper, a novel riser reactor was proposed for pyridine synthesis. Experiment result showed that the yield of pyridine and 3-picoline decreased, but the selectivity of pyridine over 3-picoline increased compared to turbulent fluidized-bed reactor. Based on experimental data, a modified kinetic model was used for the determination of optimal operating condition for riser reactor. The optimal operating condition of riser reactor given by this modified model was as follows: The reaction temperature of 755 K, catalyst to feedstock ratio(CTFR) of 87, residence time of 3.8 s and initial acetaldehydes concentration of 0.0029 mol·L^(-1)(acetaldehydes to formaldehydes ratio by mole(ATFR) of 0.65 and ammonia to aldehydes ratio by mole(ATAR) of 0.9, water contention of 63 wt%(formaldehyde solution)). 展开更多
关键词 反应堆 反应条件 合成 运动模型 操作条件 甲醛溶液 反应温度 流体化
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