Biogas, composed of CO2 and CH4, presents promising, underexplored pathways for greenhouse gas mitigation by sequestering carbon into valuable carbon nanomaterials. Carbon nanofibers (CNFs) and nanotubes (CNTs) are versatile materials that have lifespans significantly longer than conventional chemical products. Biogas conversion to carbon nanomaterials typically relies on dry reforming of CH4 (DRM) with CO2 to produce syngas, which then reacts to form C(s) via the Boudouard and CO hydrogenation reactions. These processes require temperatures >800ºC to limit coke deposition and overcome the thermodynamic stability of CH4 and CO2. Discretizing DRM and sequestration circumvents these limitations and enhances solid carbon yield while reducing energy consumption. Here, we present several tandem catalytic strategies for CO2-assisted and CH4 into carbon nanomaterials. A one-pot tandem strategy for biogas conversion to CNFs was studied, wherein sequential catalyst beds of Ni/MCM-41and Co12K5/CeO2 catalysts were used for the DRM and sequestration steps, respectively, within a single reactor at 600 ºC. This process achieved a catalyst weight gain (CWG) of 1.3 mg CNF/mg Co12K5/CeO2 after 5 h. The same catalysts were employed in two separate, sequentially coupled DRM and sequestration reactors, operating at 600ºC and 450ºC, respectively, yielding a maximum CWG of 7.0 mg CNF/mg Co12K5/CeO2. Finally, a tandem plasma catalytic-thermocatalytic (PC-TC) scheme was tested. CO2 and CH4 were activated within a non-thermal plasma reactor operating at 7 W, before being fed into the sequestration reactor, and a CWG of 0.8 mg CNF/mg Co12K5/CeO2 was observed. This tandem PC-TC approach was extended to CO2-assisted C2H6 sequestration into CNTs with the plasma reactor operating at 5 W and the sequestration reactor operating at 750ºC with a Co/γ-Al2O3 catalyst. A CWG of 1.2 mg CNT/ Co/γ-Al2O3 was obtained. Finally, analyses of the energy costs and CO2 footprints associated with these processes confirm the advantages of the tandem reactor framework.