期刊文献+

膜式水冷壁结构燃磷塔的开发与传质传热的数值模拟(Ⅰ)模型建立 被引量:1

Simulation of mass and heat transfer in new phosphoric acid tower with circular water wall(Ⅰ) Model development
下载PDF
导出
摘要 针对热法磷酸生产中一方面要求外部供热,另一方面又浪费自身燃烧热的现状,提出能回收余热的新工艺,开发成功膜式水冷壁结构新型燃磷塔.建立了考虑新型燃磷塔内流动、燃烧、传热过程的三维数学模型,通过数值模拟得到塔内湍流场、温度场和组分浓度场的分布.模拟结果显示,燃磷塔内存在明显的涡流射流结构,磷的燃烧主要在喷磷枪雾化角范围内,塔内最高燃烧温度约为1790K,出现在喷磷枪轴线上偏离燃磷塔中心的一侧.烟气出口温度约为970K,与测量值符合较好. To avoid the energy waste in the production of furnace grade phosphoric acid, a new phosphoric acid tower with circular water wall was designed, which could recover waste heat to produce superheated steam. A three dimensional mathematical model of phosphorus combustion in the new phosphoric acid tower was developed by incorporating the k-ε turbulence model, eddy dissipation turbulent combustion model and P-1 radiation heat transfer model. The streamline field distribution, temperature distribution and species concentration distribution were predicted by numerical simulation. The results showed that phosphorus combustion mainly took place in the injection zone of atomized phosphorus, and the maximum combustion temperature and exit temperature were 1790 K and 970 K respectively which conformed well to practical data.
出处 《化工学报》 EI CAS CSCD 北大核心 2006年第5期1107-1113,共7页 CIESC Journal
关键词 燃磷塔 节能 数学模型 数值模拟 phosphoric acid tower energy conservation mathematical model numerical simulation
  • 相关文献

参考文献10

  • 1Hudson R B,Mo K.Methods of preparing ultraphosphoric acid:US,Patent 4309394.1982
  • 2Kobayashi Toshitukasa.Process units of phosphoric acid.JP,5484890.1979
  • 3Shute J F,Rosenhouse H.Heat recovery in the manufacture of phosphoric acid:EU,0129533.1984
  • 4Liu Baoqing(刘宝庆).Development of two kinds of new special reactors and research on their mass and heat transfer models[D].Hangzhou:Zhejiang University,2005
  • 5Launder B E,Spalding D B.Lectures in Mathematical Models of Turbulence.London:Academic Press,1972
  • 6Magnussen B F,Hjertager B H.On mathematical models of turbulent combustion with special emphasis onsoot formation and combustion//Proc.16th Int.Symp.on Combustion.London:The Combustion Institute,1976:364-370
  • 7Siegel R,Howell J R.Thermal Radiation Heat Transfer.Washington:Hemisphere,1992
  • 8John D Anderson.Computational Fluid Dynamics-the Basics with Applications.Beijing:Tsinghua University Press,2002
  • 9Tao Wenquan(陶文铨).Numerical Heat Transfer (second edition).Xi'an:Xi'an Jiaotong University Press,2002
  • 10Zha Guorong (查国荣),Chen Jiayong (陈家镛).Principle and Application of Transmission Process.Beijing:Metallurgical Industry Press,1997

同被引文献10

  • 1ZhangYikun(张义堃) LiuBaoqing(刘宝庆) JiangJialing(蒋家羚) LinXinghua(林兴华).Currentsituation and prospect of recovery and utilization of yellowphosphorus tail gas.化工机械,39(3):389-394.
  • 2Ma Liping,Ning Ping,Zhang Yuanyuan,Wang Xueqian.Experimental and modeling of fixed-bed reactor for yellowphosphorous tail gas purification over impregnated activatedcarbon[J].Chemical Engineering Journal,2008,137(3):471-479.
  • 3Zuo Jianguo(左建国).Method for the production of95%formic acid[P]:CN,200610200857.3.2007-07-11.
  • 4Luo Yun,Deng Min,Cao Zhengxiang.The process ofproducing formic acid with phosphoric acid extracted andsodium formate[P]:International Application No.PCT/CN,2007/071087.2009-03-05.
  • 5Liu Baoqing(刘宝庆),Zhang Yikun(张义堃),JiangJialing(蒋家羚),Lin Xinghua(林兴华),He Jinlin(何锦林),Liang Huili(梁慧力).System for the continuousproduction of high quality formic acid with sodium formateacidized by polyphosphoric acid[P]:CN,201120201092.1.2011-06-15.
  • 6Liu Baoqing(刘宝庆),Qian Luyan(钱路燕),LinXinghua(林兴华),Jiang Jialing(蒋家羚),He Jinlin(何锦林),Liang Huili(梁慧力).Multilevel acidificationdevice for the continuous production of formic acid[P]:CN,201110160380.1.2011-06-15 .
  • 7晏明朗.磷化工发展必走创新和循环经济之路(1)——黄磷尾气回收净化利用[J].无机盐工业,2009,41(10):1-3. 被引量:9
  • 8段春月.黄磷尾气综合利用现状及建议[J].云南化工,2010,37(2):53-56. 被引量:4
  • 9韩海波.甲酸与六偏磷酸钠生产市场状况及联产新工艺[J].贵州化工,2001,26(1):5-9. 被引量:6
  • 10宁平,任丙南.黄磷尾气的综合利用及净化途径探讨[J].云南环境科学,2003,22(B03):149-151. 被引量:25

引证文献1

二级引证文献4

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部