| 注册
首页|期刊导航|电力科技与环保|300MW CFB锅炉旋风分离器改造数值模拟研究

300MW CFB锅炉旋风分离器改造数值模拟研究

姜恒 谢玉婷 刘海玉 牛俊天

电力科技与环保2024,Vol.40Issue(1):87-94,8.
电力科技与环保2024,Vol.40Issue(1):87-94,8.DOI:10.19944/j.eplep.1674-8069.2024.01.011

300MW CFB锅炉旋风分离器改造数值模拟研究

Numerical simulation study on the enhancement of cyclone separator in CFB boilers

姜恒 1谢玉婷 1刘海玉 1牛俊天1

作者信息

  • 1. 太原理工大学,山西 太原 030024
  • 折叠

摘要

Abstract

Cyclone separator separation performance can significantly affect circulating fluidized bed boiler operation.In order to solve the problem of poor separator performance of cyclone separator in a 300 MW circulating fluidized bed boil-er,based on the Euler-Lagrange framework,firstly,a full loop geometric model of the furnace,cyclone separator and re-turn valve of the 300 MW circulating fluidized bed boiler was established by ug software according to the actual size of 1:1,and then the boundary conditions were set according to the actual parameters,and then numerical simulation was carried out by Barracuda software.Numerical simulations were carried out by Barracuda software to analyze the effects of the flue inlet parameters of the cyclone separator:inlet flue height,inlet flue width,inlet downward tilt angle and the in-sertion depth of the center cylinder on the cyclone separator efficiency and pressure drop.The deviation between the simulated and actual values of the pressure in the furnace chamber is within 5%,and the simulation results are relatively accurate.Considering the separation efficiency,pressure drop and wear and tear of the separator,two modification schemes are proposed.Simulation results show that the two schemes can improve the cyclone separator separation per-formance at all loads,the efficiency of Scheme Ⅰ at full load is improved by 0.26%and the pressure drop is reduced by 13.1 Pa compared with that before the retrofit,and the efficiency of Scheme Ⅱ at full load is improved by 0.24%and the pressure drop is reduced by 53.7 Pa compared with that before the retrofit;with the reduction of the load,the efficiency improvement is not obvious gradually,and the efficiency improvement is not obvious at 300 MW,260 MW and 160 MW loads,Scheme Ⅰ improves the efficiency of the separator by 0.26%,0.178%,and 0.023%,respectively,and Scheme Ⅱ improves it by 0.24%,0.174%,and 0.02%,respectively.

关键词

300MW/CFB锅炉/旋风分离器/数值模拟

Key words

300 MW/CFB boilers/cyclone separator/numerical simulation

分类

能源科技

引用本文复制引用

姜恒,谢玉婷,刘海玉,牛俊天..300MW CFB锅炉旋风分离器改造数值模拟研究[J].电力科技与环保,2024,40(1):87-94,8.

基金项目

新型电力系统运行与控制全国重点实验室项目(SKLD23KM25) (SKLD23KM25)

电力科技与环保

1674-8069

访问量0
|
下载量0
段落导航相关论文