蒸汽重整
二氧化碳重整
甲烷转化炉
放热反应
甲烷
制氢
催化重整
部分氧化
吸热过程
合成气
废物管理
烟气
天然气
工艺工程
化学工程
原材料
氢
化学
工程类
有机化学
吸附
作者
Zahra Arab Aboosadi,M. Farhadi Yadecoury
标识
DOI:10.1515/ijcre-2019-0108
摘要
Abstract Tri- reforming is the main key for thermal intensification of hydrogen production based process. The arrangement of dry reforming, endothermic steam reforming, and exothermic partial oxidation make up a tri-reforming procedure. The benefit of the tri-reforming procedure is that it can be practical for energy supply for the dry and steam reforming reactions from the production of heat from the exothermic oxidation reaction. Some scientists have reviewed its usage with biogas feedstock to generate synthesis gas because the tri-reforming procedure employs CO 2 . Furthermore, the tri-reforming procedure is a technique to cut CO 2 emissions in flue stack gases. In yielding synthesis gas from biological gas, two chief functioning issues give the anticipated H 2 /CO ratio that consists of the extreme conversion of methane and also prevents coke deposition. The wanted H 2 / CO ratio differs with the wanted usage for the synthesis gas. In the present paper, the published studies from 2001 until now in three classifications have been chosen for further discussion. Finally, various suggestions have been proposed to escape catalyst deactivation due to the high-temperature nature of tri-reforming as a guideline for further investigations.
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