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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.

Thermally Intensification of Steam Reforming Process by Use of Methane Tri-Reforming: A Review