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Heat recovery within Na-O-H thermochemical cycle for hydrogen production

عنوان مقاله: Heat recovery within Na-O-H thermochemical cycle for hydrogen production
شناسه ملی مقاله: ISME31_318
منتشر شده در سی و یکمین همایش سالانه بین­ المللی مهندسی مکانیک ایران و نهمین همایش صنعت نیروگاهی ایران در سال 1402
مشخصات نویسندگان مقاله:

Matin Aslani Yekta - Sustainable Energy Research Group (SERG), School of Mechanical Engineering, Iran University of Science andTechnology, Tehran, Iran
Samane Ghandehariun - Sustainable Energy Research Group (SERG), School of Mechanical Engineering, Iran University of Science andTechnology, Tehran, Iran

خلاصه مقاله:
Hydrogen is a green energy carrier capable of storingenergy in chemical form in order to meet industrialand energy demands. Hydrogen is very reactive,cannot be found purely in nature, and needs to beproduced using special methods. In this paper, a Na-O-H thermochemical water splitting cycle forhydrogen production was investigated. The Na-O-Hcycle was modelled in Aspen Plus for the productionof ۱ kg/s of hydrogen, and then stream results wereused for heat exchanger network design and heatrecovery within the cycle. A designed network usingpinch logic can reduce the external heat requirementof cycle streams by ۸۳.۸۶% and the cooling load by۸۶.۷%. The total external energy requirement wasreduced by ۸۵.۳۴%. This reduction can make theNAOH cycle more feasible by reducing itsdependence on external heating and cooling loads.

کلمات کلیدی:
Hydrogen production, Thermochemicalwater splitting, Pinch analysis, Heat exchangernetwork design

صفحه اختصاصی مقاله و دریافت فایل کامل: https://civilica.com/doc/1668732/