Evaluation of silica membrane performance in various designs for hydrogen separation
محل انتشار: شانزدهمین کنگره ملی مهندسی شیمی ایران
سال انتشار: 1397
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 513
فایل این مقاله در 5 صفحه با فرمت PDF قابل دریافت می باشد
- صدور گواهی نمایه سازی
- من نویسنده این مقاله هستم
استخراج به نرم افزارهای پژوهشی:
شناسه ملی سند علمی:
NICEC16_453
تاریخ نمایه سازی: 7 خرداد 1398
چکیده مقاله:
Hydrogen as a high-quality and clean energy carrier has attracted renewed and ever-increasing attention around the world in recent years, mainly due to developments in fuel cells and environmental pressures including climate change issues. The major purpose of present study, is investigation of the Silica membrane performance for various configurations, namely; single stage, single-stage with retentate recycle and countercurrent recycle cascade (CRC), during separation of hydrogen from reforming products. To this aim, a black-box model was developed using PROII software version 10 and its validation was carried out by comparing the simulation results with experimental data. After simulation validation, for hydrogen separation, various configurations of silica membrane process (single stage, Single-stage with retentate recycle configuration and countercurrent recycle cascade (CRC) multistage) were compared and the best results were achieved for CRC configuration.
کلیدواژه ها:
نویسندگان
Mostafa Jafari
Department of Chemical Engineering, Tehran University, Tehran-Iran
Kamran Ghasemzadeh
Department of Chemical Engineering, Urmia University of Technology, Urmia - Iran.
Hossein Soltanalizadeh maleki
Department of Chemical Engineering, Urmia University of Technology, Urmia - Iran.