固定化微生物两级还原耦合络合吸收工艺脱除NO<sub>x</sub>的动力学研究

林添明; 周作明; 荆国华

欢迎来到能源电力期刊网！

English Version 读者登录期刊登录

您当前的位置：

首页 >

文章列表页 >

固定化微生物两级还原耦合络合吸收工艺脱除NO_x的动力学研究

热能科学研究 | 更新时间：2025-09-28

- 固定化微生物两级还原耦合络合吸收工艺脱除NO_x的动力学研究
- Kinetics study on chelate absorption coupled with two-stage bio-reduction by immobilized microorganisms in NO_x removal
- 热力发电 2013年42卷第8期页码：49-54
- 作者机构：
  
  华侨大学化工学院
- 作者简介：
- 基金信息：
- DOI：
  中图分类号： X511
- 纸质出版：2013
- 稿件说明：
移动端阅览
林添明, 周作明, 荆国华. 固定化微生物两级还原耦合络合吸收工艺脱除NO_x的动力学研究[J]. 热力发电, 2013,42(8):49-54.

LIN Tianming, ZHOU Zuoming, JING Guohua College of Chemical Engineering. Kinetics study on chelate absorption coupled with two-stage bio-reduction by immobilized microorganisms in NO_x removal[J]. Thermal power generation, 2013, 42(8): 49-54.
林添明, 周作明, 荆国华. 固定化微生物两级还原耦合络合吸收工艺脱除NO_x的动力学研究[J]. 热力发电, 2013,42(8):49-54. DOI：

LIN Tianming, ZHOU Zuoming, JING Guohua College of Chemical Engineering. Kinetics study on chelate absorption coupled with two-stage bio-reduction by immobilized microorganisms in NO_x removal[J]. Thermal power generation, 2013, 42(8): 49-54. DOI：

摘要

分析了固定化微生物两级还原耦合络合吸收工艺脱除NOx的动力学过程

建立了生物反应器内固定化微生物还原Fe(Ⅱ)EDTA-NO和Fe(Ⅲ)EDTA的生化反应模型以及固定化生物小球的扩散-反应模型。分析结果表明:固定化反硝化菌还原Fe(Ⅱ)EDTA-NO的最大反应速度γmax为6.97×10-6 mmol/(m3·s-1)

半饱和常数Km为0.001 6mmol/m3;固定化铁还原菌还原Fe(Ⅲ)EDTA的最大反应速度γ′max为6.805×10-5 mmol/(m3·s-1)

半饱和速率常数K′m为0.013 73mmol/m3;Fe(Ⅱ)EDTA-NO和Fe(Ⅲ)EDTA的微生物还原过程均由内扩散控制

后期设计运用中应着力提高小球内反应物的扩散速率。

Abstract

The kinetic process of NOxremoval by employing an integrated process of metal chelate absorption coupled with two-stage bio-reduction using immobilized microorganisms was investigated.Several models were developed such as the bio-reduction of Fe(Ⅱ)EDTA-NO and Fe(Ⅲ)EDTA in immobilized microorganisms reactor and diffusion-reaction in immobilized beads.The results indicated that the maximum reaction rate of Fe(Ⅱ)EDTA-NO reduction by immobilized bacteria in bio-reactor was 6.97×10-6 mmol/(m3.s-1)and the half-saturation constant was 0.001 6mmol/m3.The maximum reaction rate of Fe(Ⅲ)EDTA reduction by immobilized bacteria in bio-reactor was 6.805×10-5 mmol/(m3.s-1)and the half-saturation constant was 0.013 73 mmol/m3.Furthermore

the bioreduction of Fe(Ⅱ)EDTA-NO and Fe(Ⅲ)EDTA were both controlled by interior diffusion.

关键词

Keywords

references

浏览量

下载量

CSCD

文章被引用时，请邮件提醒。

提交

工具集

关联资源

暂无数据

固定化微生物两级还原耦合络合吸收工艺脱除NOx的动力学研究

Kinetics study on chelate absorption coupled with two-stage bio-reduction by immobilized microorganisms in NOx removal

DOI：

摘要

Abstract

关键词

Keywords

references

固定化微生物两级还原耦合络合吸收工艺脱除NO_x的动力学研究

Kinetics study on chelate absorption coupled with two-stage bio-reduction by immobilized microorganisms in NO_x removal