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林产化学与工业 ›› 2017, Vol. 37 ›› Issue (4): 95-102.doi: 10.3969/j.issn.0253-2417.2017.04.014

• 研究报告 • 上一篇    下一篇

废水深度处理反应器流体数值模拟与优化

盘爱享1,2, 施英乔2, 丁来保1,2, 张华兰1,2, 田庆文2, 房桂干2   

  1. 1. 中国林业科学研究院 林业新技术研究所, 北京 100091;
    2. 中国林业科学研究院 林产化学工业研究所;生物质化学利用国家工程实验室;国家林业局 林产化学工程重点开放性实验室;江苏省 生物质能源与材料重点实验室, 江苏 南京 210042
  • 收稿日期:2016-12-19 出版日期:2017-08-25 发布日期:2017-09-02
  • 通讯作者: 房桂干(1966-),男,研究员,博士生导师,主要从事制浆、造纸及水污染控制技术研究;E-mail:fangguigan@icifp.cn E-mail:fangguigan@icifp.cn
  • 作者简介:盘爱享(1979-),男,瑶族,湖南双牌人,高级工程师,博士生,主要从事环境保护技术研究和环境工程设计;E-mail:aixiangpan@163.com
  • 基金资助:
    中国林科院中央级公益性科研院所基本科研业务费专项资金(CAFYBB2016SY029)

Flow Numerical Simulation and Optimization for Wastewater Advanced Treatment Reactor

PAN Aixiang1,2, SHI Yingqiao2, DING Laibao1,2, ZHANG Hualan1,2, TIAN Qingwen2, FANG Guigan2   

  1. 1. Research Institute of Forestry New Technology, CAF, Beijing 100091, China;
    2. Institute of Chemical Industry of Forest Products, CAF;National Engineering Lab. for Biomass Chemical Utilization;Key and Open Lab. of Forest Chemical Engineering, SFA;Key Lab. of Biomass Energy and Material, Jiangsu Province, Nanjing 210042, China
  • Received:2016-12-19 Online:2017-08-25 Published:2017-09-02

摘要: 利用Fluent软件对废水深度处理反应器的流体进行三维数值模拟比较,结果表明:旋流式布水器可在反应器内形成类似于桨式搅拌器的流态形式,搅拌效果好。示踪剂模拟显示,相对于消能引流布水器,旋流式布水器粒子滞留时间更接近理论停留时间,返混更小,可作为深度处理反应器的布水器。对深度处理反应器进行数值模拟,结果显示流体经过催化剂层后只存在上向层流,无搅拌混合作用,影响药液混合反应效果,采用螺旋折流板对反应器进行优化,优化后的流速矢量发散并有旋流涡流,流体搅拌更充分,优化后速度接近原来的4倍。优化后的深度处理反应器压力降主要位于进口处,其次位于催化剂层,螺旋折流板对压力的损失可以忽略。

关键词: 深度处理反应器, 数值模拟, 旋流式布水器

Abstract: Simulated with Fluent, swirling water distributor could make a fine mixing effect as similar with the flow pattern of paddle agitator. Discrete Phase Model showed the residence time of particle in swirling water distributor is closer to theoretical value, and back flow was less than in cone water distributor. Swirling water distributor could be used as wastewater advanced reatment reactor. Numerical simulation showed that the laminar flow without mixing effect is occured after throughing catalysts layer. The advance treatment reactor was optimized with helical baffle installed up the catalysts, then the velocity vector was divergent and fluid was mixed efficient, the velocity was nearly four times than that before.The pressure drop of optimized reactor was mainly located at the inlet, then at the catalysts, the pressure loss of helical baffle could be ignored.

Key words: advanced treatment reactor, numerical simulation, water distributor

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