The computational fluid dynamics model with porosity and drag coefficient was used to describe fluid flow in an axial flow fixed bed according to the characteristics of fluid flow in the fixed-bed of the reactor. The ...The computational fluid dynamics model with porosity and drag coefficient was used to describe fluid flow in an axial flow fixed bed according to the characteristics of fluid flow in the fixed-bed of the reactor. The commercial computational fluid dynamics (CFD) code CFX was used to simulate the flow field in the axial flow fixed bed.The simulation predictions are in good agreement with experimental results of a large cold model. The influence of gas distributor on the flow field in the axial flow fixed bed was studied. A suitable gas distributor was used to attain less than 0.06 kPa radial pressure difference and less than 5.2% radial velocity difference in fixed bed.展开更多
在固定床反应器中研究了甲醇制烯烃反应过程中SAPO-34分子筛催化剂的积炭动力学,分别得到了催化剂积炭量与反应温度、剂醇比的经验关联式。结果表明,催化剂床层存在明显的积炭分布,在450℃,甲醇WHSV为15 h-1,催化剂积炭量随催化剂反应...在固定床反应器中研究了甲醇制烯烃反应过程中SAPO-34分子筛催化剂的积炭动力学,分别得到了催化剂积炭量与反应温度、剂醇比的经验关联式。结果表明,催化剂床层存在明显的积炭分布,在450℃,甲醇WHSV为15 h-1,催化剂积炭量随催化剂反应运行时间(Tim e on Stream,TOS)为25 m in时,床层入口处的积炭量平均为9.56%,而出口处的积炭量平均为3.20%,属于平行失活,积炭主要来源于甲醇生成的高碳中间体,这些中间体在生成低碳烃的同时生成积炭。从积炭的生成机理出发,得到了SAPO-34分子筛催化剂的积炭动力学机理模型,将催化剂积炭量与一定催化剂停留时间内反应过程中甲醇的转化量相关联,该模型形式同样简单,能够较好地拟合实验数据。展开更多
文摘The computational fluid dynamics model with porosity and drag coefficient was used to describe fluid flow in an axial flow fixed bed according to the characteristics of fluid flow in the fixed-bed of the reactor. The commercial computational fluid dynamics (CFD) code CFX was used to simulate the flow field in the axial flow fixed bed.The simulation predictions are in good agreement with experimental results of a large cold model. The influence of gas distributor on the flow field in the axial flow fixed bed was studied. A suitable gas distributor was used to attain less than 0.06 kPa radial pressure difference and less than 5.2% radial velocity difference in fixed bed.
文摘在固定床反应器中研究了甲醇制烯烃反应过程中SAPO-34分子筛催化剂的积炭动力学,分别得到了催化剂积炭量与反应温度、剂醇比的经验关联式。结果表明,催化剂床层存在明显的积炭分布,在450℃,甲醇WHSV为15 h-1,催化剂积炭量随催化剂反应运行时间(Tim e on Stream,TOS)为25 m in时,床层入口处的积炭量平均为9.56%,而出口处的积炭量平均为3.20%,属于平行失活,积炭主要来源于甲醇生成的高碳中间体,这些中间体在生成低碳烃的同时生成积炭。从积炭的生成机理出发,得到了SAPO-34分子筛催化剂的积炭动力学机理模型,将催化剂积炭量与一定催化剂停留时间内反应过程中甲醇的转化量相关联,该模型形式同样简单,能够较好地拟合实验数据。
