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逆流反应器中纳米材料连续热液流动合成过程建模与仿真
引用本文:张扬,马才云,刘晶晶,刘涛,王学重.逆流反应器中纳米材料连续热液流动合成过程建模与仿真[J].大连理工大学学报,2014,54(6):662-675.
作者姓名:张扬  马才云  刘晶晶  刘涛  王学重
作者单位:1. 华南理工大学 化学化工学院,广东 广州,510640
2. 利兹大学 化工与过程工程学院 颗粒科学与工程研究院,英国 利兹 LS2 9JT
3. 大连理工大学 先进控制技术研究所,辽宁 大连,116024
4. 华南理工大学 化学化工学院,广东 广州 510640; 利兹大学 化工与过程工程学院 颗粒科学与工程研究院,英国 利兹 LS2 9JT
基金项目:国家千人计划资助项目;英国工程和物理科学研究委员会资助项目(EP/E040624/1;EP/E040551/1).
摘    要:利用计算流体动力学的数值模拟来研究超临界水操作条件下,用于纳米材料合成的连续热液系统中的逆流反应器的性能.入口流量和温度是关键过程变量并在仿真过程中发生变化.预测的温度与取自相同的设计和在相同操作条件下的实验室测量数据相吻合.研究发现反应器中物料的快速混合可以通过超临界水的高流量与高入口温度,和使用非平衡的入口流量条件即超临界水的流量不等于反应物流量来实现.对比仿真还显示内管插入长度是一个反应器性能的关键控制因素,当前反应器配置下其必须小于72.5mm,以达到令人满意的混合效果.

关 键 词:逆流反应器  纳米材料热液合成  计算流体动力学  超临界水  混合  反应器设计

Modeling and simulation of counter-current reactors for continuous hydrothermal flow synthesis of nanoparticles
ZHANG Yang,MA Caiyun,LIU Jingjing,LIU Tao,WANG Xuezhong.Modeling and simulation of counter-current reactors for continuous hydrothermal flow synthesis of nanoparticles[J].Journal of Dalian University of Technology,2014,54(6):662-675.
Authors:ZHANG Yang  MA Caiyun  LIU Jingjing  LIU Tao  WANG Xuezhong
Institution:ZHANG Yang;MA Cai-yun;LIU Jing-jing;LIU Tao;WANG Xue-zhong;School of Chemistry and Chemical Engineering,South China University of Technology;Institute of Particle Science and Engineering,School of Chemical and Process Engineering,University of Leeds;Research Institute of Advanced Control Technology,Dalian University of Technology;
Abstract:Numerical simulation using computational fluid dynamics is carried out to study the performance of a counter-current reactor in a continuous hydrothermal system for nanomaterial synthesis that is operated under supercritical water condition. Inlet flowrate and temperature are the key process variables and vary in the simulation. The predicted temperatures are in good agreement with measurements taken from a laboratory rig of identical design and under the same operating conditions. It is found that fast mixing in the reactor can be achieved by high inlet temperature, high inlet flowrate of the supercritical water and using unbalanced flow conditions, i.e. the supercritical water flowrate should not be equal to that of the precursor. The comparative simulation also reveals that the insertion length of the inner tube is a key factor dictating the reactor performance, and it needs to be less than 72.5 mm in order to achieve satisfactory mixing under the current reactor configuration.
Keywords:counter-current reactor  hydrothermal synthesis of nanomaterials  computational fluid dynamics  supercritical water  mixing  reactor design
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