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基于结构参数响应的内循环流化床流体特性优化数值模拟
引用本文:朱家亮,张涛,韦朝海.基于结构参数响应的内循环流化床流体特性优化数值模拟[J].环境科学学报,2012,32(11):2732-2740.
作者姓名:朱家亮  张涛  韦朝海
作者单位:1. 华南理工大学环境科学与工程学院,广州510006 环境保护部华南环境科学研究所,广州510655
2. 华南理工大学环境科学与工程学院,广州,510006
3. 华南理工大学环境科学与工程学院,广州510006 污染控制与生态修复广东省普通高等学校重点实验室华南理工大学,广州510006
基金项目:国家自然科学基金重点项目(No.21037001); "十一五"国家科技支撑计划重点项目(No.2008BAC32B06-1); 国家高技术研究发展计划项目(No.2009AA06Z319);华南理工大学中央高校基本科研业务经费(No.2011ZP0006)
摘    要:流化床是一种结构复杂而能量转化高效的反应器型式,为了实现系统化的内循环流化床优化设计,利用欧拉-欧拉双流体模型构建了不同结构的CFD流化床模型,在分别改变高径比、导流筒与反应器的直径比和底隙高度3个结构因素的情况下,考察流化床内全流场、局部流场、液相运动速度及气含率等气液两相流的响应特性,分析结构因素及操作因素对流体运动的内在影响,阐明工程优化设计的方向.数值模拟结果表明:高径比主要影响气液流动型态,低高径比时容易出现漩涡和返混,工程中应采用导流内构件并重视气体分布装置的合理设计;导流筒与反应器的直径比主要影响液体循环速度,存在一个合理的区间,考虑流动速度与气含率,流化床直径比可取0.6~0.8,最佳取值为0.7;底隙高度影响流化床底泥区的流体运动,应约等于流化床下降区的缝隙长度.CFD模拟可作为污染控制技术工业放大和优化设计的辅助工具.

关 键 词:废水处理  内循环流化床  结构优化  流体力学  数值模拟  CFD
收稿时间:2/5/2012 12:00:00 AM
修稿时间:2012/5/10 0:00:00

Numerical optimization on hydrodynamic characteristics of internal-loop fluidized bed based upon structure parameter response relationships
ZHU Jialiang,ZHANG Tao and WEI Chaohai.Numerical optimization on hydrodynamic characteristics of internal-loop fluidized bed based upon structure parameter response relationships[J].Acta Scientiae Circumstantiae,2012,32(11):2732-2740.
Authors:ZHU Jialiang  ZHANG Tao and WEI Chaohai
Institution:1. College of Environmental Science and Technology, South China University of Technology, Guangzhou 510006;2. South China Institute of Environmental Science, Guangzhou 510655;College of Environmental Science and Technology, South China University of Technology, Guangzhou 510006;1. College of Environmental Science and Technology, South China University of Technology, Guangzhou 510006;2. Key Laboratory of Environmental Protection and Eco-Remediation of Guangdong Regular Higher Education Institutions, South China University of Technology, Guangzhou 510006
Abstract:Fluidized bed reactor is a reactor with complex internal structure and high energy transformation efficiency. A computational fluid dynamics (CFD) model for different structures by using Eulerian-Eulerian double-fluids models was established to help achieve the optimal design of internal-loop fluidized beds. With the aid of this model, the two-phase hydrodynamic characteristics of the flow field, gas holdup distribution, and liquid velocity distribution of the fluidized bed were investigated under different ratios of height to diameter, different ratios of diameters of draft tube to reactor, and height of bottom clearance and operation factors. The internal effects between structure parameters and operation factors were analyzed. The simulation results showed that the ratio of height to diameter can affect the flow pattern of liquid and gas significantly and the low ratio of height to diameter may lead to vortex and backmixing easily, suggesting that the internal draft tube should be implanted and spargers should be designed properly in engineering applications. Diameter ratio of draft tube to reactor has a large effect on liquid recirculation velocity, and thus has a reasonable range. Considering the liquid circulation velocity and gas holdup, the appropriate range of diameter ratio of draft tube to reactor is from 0.6 to 0.8, with 0.7 the optimal. The height of bottom clearance can affect local flow structure in bottom zone, and its height should be equal to the length of the downcomer. This study indicates that the CFD simulation can be used as a supportive approach for optimizing design and pilot test of reactors in pollution control field.
Keywords:wastewater treatment  internal loop fluidized bed  optimum design  hydrodynamics  numerical simulation  CFD (Computational Fluid Dynamics)
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