In this perspective, I discuss a few basic concepts in fundamental mechanistic studies of electrochemical carbon dioxide reduction. With the looming global environmental crisis, electrochemical CO 2 reduction (CO 2 R) is a hot topic. Excellent perspectives on mechanistic studies 1-3 , practical vapor-fed devices 4 , and technoeconomic and system-level analyses 5-7 have come out in the past few years, all with compelling visions for the future. We can also harken back to Hori's timeless review of his work over several decades 8 , which seeded many of the impressive advances today. But as the French maxim says: parfois, il faut reculer pour mieux sauter. Here, I showcase a few basic concepts in the fundamental mechanistic studies of CO 2 R. What computational electrocatalysis can and cannot do In heterogeneous catalysis, periodic density functional theory (DFT) simulations have really enabled us to computationally explore reaction mechanisms. For electrocatalysis, the "computational hydrogen electrode" model is our standard method to determine reaction thermodynamics 9. This method trivially translates simulations in vacuum to potential-dependent energetics, without requiring we simulate explicitly the ions or potential. Our models of the electrolyte and electrochemical reaction barriers, in contrast, are far from convergent. Our field abounds with different approaches towards the electrolyte: implicit continuum models, explicit ab initio ones, or a hybrid of the two (Fig. 1a) 10. We also have multiple ways to obtain the potential and the potential dependence of the reaction energetics 11. While continuum approximations give us huge reductions in computational cost, we see significant deviations in solvation energies determined with implicit vs. dynamic explicit water models 12. Furthermore, different ways to set up the applied potential result in differences in the computed reaction energetics 13. All these challenges could contribute to the wide range in the computed energetics and mechanisms towards the various C 2 products 1. Despite the difficulties in an ab initio treatment of electrochemical reaction barriers, we do need kinetics for mechanistic understanding. Case in point: our evolving understanding of CO (2) R to CH 4 on Cu 14. A thermodynamic analysis showed a proton-electron transfer to *CO to form *CHO to be the rate-limiting step. Considering the corresponding barriers across different materials, we suggested the transition state of this process to be the descriptor of activity. But when we simply consider the kinetics of electrochemical reactions with multiple proton-electron transfers, we see that this step cannot be rate limiting on Cu. The corresponding Tafel plots have defining features that depend on the symmetry factor β (0 < β < 1) for the rate-limiting step, as well as the number of proton-electron transfers preceding it, n. Figure 1b shows the Tafel slopes and the effect of pH on the overpotential for alkaline solutions, where H 2 O as the proton donor. Experiments show