“…Experimentally, a number of heteroge- neous catalysts were examined such as Cu−Co-based catalyst, 9 M/SiO 2 (M = Pd and Rh), 10 Co−Pd/TiO 2 , 11 Fe/ZnO, 12 Cumodified ZSM-5, 13 Zn-modified H-ZSM-5, 14 and montmorillonite (MMT) supported oxides (ZnO, CeO 2 , MnO 2 −ZnO, CeO 2 −MnO 2 , and CeO 2 −ZnO). 15 Computationally, density functional theory (DFT)-guided mechanistic understanding and catalyst design were conducted over a series of heterogeneous catalysts such as ZnO (1010), Cu/ZnO (1010), and Fe/ZnO (1010) surfaces, 12 CeO 2 (111) and ZnO (1010) surfaces, 15 Au(I)-ZSM-5, 16 Cu(111) surface, 17 Zn-doped ceria, 18 (ZnO) 3 −In 2 O 3 interface, 19 M-exchanged MFI zeolites (M = Be, Co, Cu, Mg, Mn, Zn), 20 Cu-modulated BEA, MFI, MOR, and TON zeolites, 21 Zn-modified H-ZSM-5, 22 MFI zeolite, 23 undoped/doped In 2 O 3 (110) surfaces, 24 and dual sites on CeO 2 (110) surfaces. 25 For CH 4 + CO 2 = CH 3 COOH, the catalytic cycle generally involves CH 4 activation and dissociation, C−C coupling between CH 3 anion and gaseous/activated CO 2 , proton transfer for CH 3 COOH formation, and desorption of CH 3 COOH from the catalyst.…”