{"title":"Mathematical modelling of simultaneous hydrogenation of benzene and ethane dehydrogenation in a membrane reactor","authors":"Dongdong Zhao , Jingwei Meng , Xuemei Lin","doi":"10.1016/j.csite.2025.106133","DOIUrl":null,"url":null,"abstract":"<div><div>Membrane reactors for hydrogen production are interesting devices that allow us to perform dehydrogenation and hydrogenation reactions in one system simultaneously. In this work, a two-dimensional mathematical model has been developed for the investigation of mass and heat transfer in a membrane reactor where both ethane dehydrogenation reaction and benzene hydrogenation are carried out at the same time. The effect of inlet temperatures and porosity in both sides of the membrane reactor on the performance of the system has been investigated. The results showed that the benzene conversion is 0.14 %, 0.18 %, and 0.07 % at tube side inlet temperatures of 700 K, 800 K, and 900 K. It means that there is an optimum inlet temperature in the tube side of the membrane reactor. The increase in porosity from 0.3 % to 0.8 % in the shell side results in a decrease in the conversion of both benzene and ethane in the system. Also, the outlet temperatures were decreased in both sides with the increase of shell side porosity.</div></div>","PeriodicalId":9658,"journal":{"name":"Case Studies in Thermal Engineering","volume":"71 ","pages":"Article 106133"},"PeriodicalIF":6.4000,"publicationDate":"2025-04-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Case Studies in Thermal Engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2214157X25003934","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"THERMODYNAMICS","Score":null,"Total":0}
引用次数: 0
Abstract
Membrane reactors for hydrogen production are interesting devices that allow us to perform dehydrogenation and hydrogenation reactions in one system simultaneously. In this work, a two-dimensional mathematical model has been developed for the investigation of mass and heat transfer in a membrane reactor where both ethane dehydrogenation reaction and benzene hydrogenation are carried out at the same time. The effect of inlet temperatures and porosity in both sides of the membrane reactor on the performance of the system has been investigated. The results showed that the benzene conversion is 0.14 %, 0.18 %, and 0.07 % at tube side inlet temperatures of 700 K, 800 K, and 900 K. It means that there is an optimum inlet temperature in the tube side of the membrane reactor. The increase in porosity from 0.3 % to 0.8 % in the shell side results in a decrease in the conversion of both benzene and ethane in the system. Also, the outlet temperatures were decreased in both sides with the increase of shell side porosity.
期刊介绍:
Case Studies in Thermal Engineering provides a forum for the rapid publication of short, structured Case Studies in Thermal Engineering and related Short Communications. It provides an essential compendium of case studies for researchers and practitioners in the field of thermal engineering and others who are interested in aspects of thermal engineering cases that could affect other engineering processes. The journal not only publishes new and novel case studies, but also provides a forum for the publication of high quality descriptions of classic thermal engineering problems. The scope of the journal includes case studies of thermal engineering problems in components, devices and systems using existing experimental and numerical techniques in the areas of mechanical, aerospace, chemical, medical, thermal management for electronics, heat exchangers, regeneration, solar thermal energy, thermal storage, building energy conservation, and power generation. Case studies of thermal problems in other areas will also be considered.