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Selective phenol methylation to 2,6-dimethylphenol in a fluidized bed of iron-chromium mixed oxide catalyst with o–cresol circulation

机译:在邻甲酚循环的铁铬混合氧化物催化剂流化床中选择性苯酚甲基化为2,6-二甲基苯酚

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Background 2,6-dimethylphenol (2,6-DMP) is a product of phenol methylation, especially important for the plastics industry. The process of phenol methylation in the gas phase is strongly exothermic. In order to ensure good temperature equalization in the catalyst bed, the process was carried out using a catalyst in the form of a fluidized bed - in particular, the commercial iron-chromium catalyst TZC-3/1. Results Synthesis of 2,6-dimethylphenol from phenol and methanol in fluidized bed of iron-chromium catalyst was carried out and the fluidization of the catalyst was examined. Stable state of fluidized bed of iron-chromium catalyst was achieved. The measured velocities allowed to determine the minimum flow of reactants, ensuring introduction of the catalyst bed in the reactor into the state of fluidization. Due to a high content of o-cresol in products of 2,6-dimethylphenol synthesis, circulation in the technological node was proposed. A series of syntheses with variable amount of o-cresol in the feedstock allowed to determine the parameters of stationary states. Conclusion A stable work of technological node with o-cresol circulation is possible in the temperature range of350-380°C, and o-cresolin/phenolin molar ratio of more than 0.48. Synthesis of 2,6-DMP over the iron-chromium catalyst is characterized by more than 90% degree of phenol conversion. Moreover, the O-alkylation did not occur (which was confirmed by GC-MS analysis). By applying o-cresol circulation in the 2,6-DMP process, selectivity of more than 85% degree of 2,6-DMP was achieved. The participation levels of by-products: 2,4-DMP and 2,4,6-TMP were low. In the optimal conditions based on the highest yield of 2,6-DMP achieved in the technological node applying o-cresol circulation, there are 2%mol. of 2,4-DMP and 6%mol. of 2,4,6-TMP in the final mixture, whereas 2,4,6-TMP can be useful as a chain stopper and polymer?s molar mass regulator during the polymerization of 2,6-DMP.
机译:背景技术2,6-二甲基苯酚(2,6-DMP)是苯酚甲基化的产物,对塑料工业尤为重要。气相中的苯酚甲基化过程强烈放热。为了确保催化剂床中良好的温度均衡,该方法使用流化床形式的催化剂,特别是市售铁铬催化剂TZC-3 / 1进行。结果在铁铬催化剂的流化床中,由苯酚和甲醇合成了2,6-二甲基苯酚,并考察了催化剂的流化性能。实现了铁铬催化剂流化床的稳定状态。测得的速度可以确定反应物的最小流量,从而确保将反应器中的催化剂床引入流化状态。由于2,6-二甲基苯酚合成产物中邻甲酚含量高,因此提出了在技术节点中进行循环的建议。原料中一系列具有可变邻甲酚含量的合成方法可以确定稳态参数。结论在350-380°C的温度范围内,邻甲苯酚/酚精摩尔比大于0.48时,邻甲苯酚循环的工艺节点可以稳定工作。在铁-铬催化剂上合成2,6-DMP的特征在于苯酚转化率超过90%。此外,未发生O-烷基化(通过GC-MS分析确认)。通过在2,6-DMP工艺中使用邻甲酚循环,可以实现2,6-DMP选择性大于85%的选择性。副产物2,4-DMP和2,4,6-TMP的参与水平较低。在基于使用邻甲酚循环的技术节点中实现的最高2,6-DMP收率的最佳条件下,存在2%摩尔。 2,4-DMP和6%mol。最终混合物中的2,4,6-TMP为2,4,6-TMP,在2,6-DMP聚合过程中,2,4,6-TMP可用作链终止剂和聚合物的摩尔质量调节剂。

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