limits. One potentially useful technology for reducing CO 2 is to directly capture it from power plant flue gas, as well as from other stationary emissions sources. Three different technological approaches for capture of CO 2 from stationary sources are currently being investigated; post-combustion, pre-combustion, and oxyfuel combustion capture. [1] For post-combustion capture, CO 2 is removed from the flue gas which is emitted after combustion of the fuel in air. Pre-combustion CO 2 capture can be performed following gasification of the coal, prior to combustion producing a high-pressure flue gas containing H 2 and CO 2. Based on the respective flue gas compositions, it is necessary for a postcombustion CO 2 adsorbent to exhibit a high CO 2 /N 2 /H 2 O selectivity, and for a pre-combustion adsorbent to have a high CO 2 /H 2 /H 2 O selectivity. [2] Numerous solid or liquid-based CO 2 sorbents have been examined, including zeolites, [3] activated carbons, [4] metal-organic frameworks (MOFs), [5] ionic liquids, [6] polymeric membranes, [7] microporous polymers, [8] and mesoporous silica. [9] Amine-tethered adsorbents exhibit particularly useful attributes, such as wide temperature operating windows, as a result of their CO 2sorbent interaction energies that range from 50 to 100 kJ mol −1. However, amines have limits for large-scale field applications due to the associated large energy penalty for sorbent regeneration, and their low thermal stability over time. [10] MOFs based on unsaturated metal sites have exhibited attractive CO 2 uptake capacities, in addition to acting as stable supports for amines. [11] However, to date their scale-up remains limited. Activated carbons are attractive for CO 2 capture due to their low-cost and overall abundance, in particular when derived from biomassbased precursors, or from coal and oil products. Carbons derived from pyrolysis and activation of yeast, [12] fungi, [13] palm shells, [14] coconut shells, [15] pine nut shells, [16] soya bean dregs, [17,18] bamboo, [19] wheat flour, [20] and leaves [21] have been employed for carbon capture. [22] Carbons prepared from such waste precursors stand out as economically promising and sustainable, but generally fall short of meeting the CO 2 capture performance metrics set by the more complex and expensive systems such as MOFs. Hence, the pressing challenge is to create an inexpensive "green" activated carbon, but with stateof-the-art CO 2 capture performance. This is the first report of Pore size distribution and surface chemistry of bio-derived (milk) microporous dominated carbon "MDC" is synergistically tuned, allowing for promising carbon capture in a dry CO 2 atmosphere and in mixed H 2 O-CO 2. The capture capacity is attributed to the synergy of a large total surface area with an ultramicroporous and microporous texture (e.g., S tot 1889 m 2 g −1 , S mic 1755 m 2 g −1 , S ultra 1393 m 2 g −1), and a high content of nitrogen and oxygen heteroatom moieties (e.g., 5 at% N, 10.5 at% O). Tailored two-step low-temperature pyrolysischem...