“…First, the combination of SRM and DRM allows for better control over the hydrogen-to-carbon monoxide (H 2 /CO) ratio in the syngas. , DRM typically yields a near-equal H 2 /CO ratio of 1:1, which may not always be ideal for certain downstream processes. However, incorporation of steam in BRM enables the adjustment of the H 2 /CO ratio toward a higher hydrogen content (i.e., H 2 /CO = 2:1). , This flexibility in tailoring the syngas composition enhances the versatility and suitability of the produced syngas for various industrial applications, such as Fischer–Tropsch synthesis or methanol production. ,, Besides, the presence of steam mitigates coke formation on the catalyst surface, a common issue in DRM, resulting in improved catalyst stability and longevity. ,,– These advantages position BRM as a promising pathway for CCU, warranting further investigation and development.…”