Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions

Jiajin Zhang; Zhigang Lei; Jianwei Li; Biaohua Chen

doi:10.1016/j.cjche.2014.06.005

Your Location：

Home >

Browse articles >

Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions

第四届整体式结构化催剂与反应器国际会议专栏 | Updated：2026-01-06

- Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions
- Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions
- 中国化学工程学报（英文版） 2014年22卷第8期页码：843-853
- Affiliations：
  
  State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology,Beijing,China,100029
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2014.06.005
  中图分类号：
- 纸质出版：2014
- Accepted：
Scan QR Code
Jiajin Zhang, Zhigang Lei, Jianwei Li, 等. Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions[J]. 中国化学工程学报（英文版）, 2014,22(8):843-853.

Jiajin Zhang, Zhigang Lei, Jianwei Li,Biaohua Chen, Jiajin Zhang, Zhigang Lei, Jianwei Li, Biaohua Chen. Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions[J]. Chin.J.Chem.Eng., 2014, 22(8): 843-853.
Jiajin Zhang, Zhigang Lei, Jianwei Li, 等. Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions[J]. 中国化学工程学报（英文版）, 2014,22(8):843-853. DOI： 10.1016/j.cjche.2014.06.005.

Jiajin Zhang, Zhigang Lei, Jianwei Li,Biaohua Chen, Jiajin Zhang, Zhigang Lei, Jianwei Li, Biaohua Chen. Simulation of a Reverse FlowReactor for the Catalytic Combustion of Lean Methane Emissions[J]. Chin.J.Chem.Eng., 2014, 22(8): 843-853. DOI： 10.1016/j.cjche.2014.06.005.

摘要

Abstract

Thiswork is focused on the performance prediction of pilot scale catalytic reverse flow reactors used for combustion of lean methane-air mixtures. An unsteady one-dimensional heterogeneous model for the reactor was established to account for the influence of the reactor wall on the heat transfer. Results of the simulation indicate that feed concentration

switch time and compensatory temperature impose important influence on the performance of the reactor. The amount of the heat extracted from the mid-section of the reactor can be optimized via adjusting the parameters mentioned above. At the optimal operating conditions

i.e. switching time of 400 s

feed concentration of 1% (by volume)

and insulation layer temperature of 343 K

the axial temperature of the reactor revealed a comparatively symmetrical "saddle" distribution

indicating a favorable operating status of the catalytic reverse flow reactor.

关键词

Keywords

references

浏览量

Downloads

CSCD

文章被引用时，请邮件提醒。

Submit

工具集

关联资源

Preparation of anodic catalysts via in situ exsolution of Pt nanoparticles for a methane oxidation enhanced SOEC process

Research progress on the monolithic catalyst for hydrogenation of CO2 to methane

Preparation of MoO3/γ-Al2O3 sulfur-resistant methanation catalyst with segmented plasma fluidized bed

Investigation on the reducing parameters of the Helmholtz energy equation of state for methane/methanol binary with VLE data

Structural modification and heat transfer enhancement on HKUST-1 for adsorbed natural gas