Mathematical modelling and simulation of nitrite hydrogenation in a membrane microreactor

被引:2
|
作者
Pishnamazi, Mahboubeh [1 ,2 ,3 ]
Ghadiri, Mahdi [4 ,5 ]
Shirazian, Saeed [3 ]
机构
[1] Duy Tan Univ, Inst Res & Dev, Da Nang 550000, Vietnam
[2] Duy Tan Univ, Fac Pharm, Da Nang 550000, Vietnam
[3] Univ Limerick, Bernal Inst, Dept Chem Sci, Limerick, Ireland
[4] Ton Duc Thang Univ, Informetr Res Grp, Ho Chi Minh City, Vietnam
[5] Ton Duc Thang Univ, Fac Appl Sci, Ho Chi Minh City, Vietnam
关键词
Modelling; Hydrogenation; Nitrite; Hydrogen; Membrane reactor; MASS-TRANSFER; NITRATE; WATER; REMOVAL; CATALYSTS; POROSITY; SUPPORT; PD;
D O I
10.1016/j.ijhydene.2020.05.210
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Nitrite hydrogenation using heterogeneous catalysis is an important process for purification of wastewater or potable water. The main aim of this study is to explore a new mechanistic model and simulation for a heterogeneously catalysed reaction in a micro- porous catalytic layer. The system studied involves a liquid solution containing certain amount of nitrite, and a membrane reactor in which the nitrite penetrates into the catalytic layer to react with hydrogen. The developed model considers coupling between equations of momentum transfer in free and porous media and convection-diffusion of nitrite. It was found that there is great agreement between measured data and modelling values. Increasing velocity was the main reason for reduction of nitrite conversion and also there was a slight increase in nitrite conversion with increasing the thickness and porosity of catalytic layer. Furthermore, it was found that the diffusion mass transfer mechanism is favourable for nitrite hydrogenation while convective mass transfer of fluid flow has negative impact on nitrite hydrogenation. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21555 / 21566
页数:12
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