Separation of CO 2 in the flue gas emitted from coal-fired power plants is the first technological step toward reducing the CO 2 concentration in atmosphere, and eventually for mitigating the global climate change. 1,2 In this respect, postcombustion processes employing CO 2 -absorbing agents or CO 2 sorbents have been actively developed. 3 Aqueous 30 wt % monoethanolamine (MEA, HO(CH 2 ) 2 NH 2 ) solution is a representative sorbent, which quickly absorbs and separates CO 2 from flue gas through forming an MEA carbamate salt [HO(CH 2 ) 2 NH 3 + ][HO(CH 2 ) 2 NHCOO − ]. 4-6 In this way, more than 95% of CO 2 in flue gas can be captured with preventing CO 2 from being emitted to atmosphere. The current problem underlying in the aqueous amine sorbent process is that the stripping step consumes a large amount of energy in regenerating the amines for repeated usages. Therefore, extensive research efforts are currently being devoted to developing efficient amines or their mixtures with aiming at enhancing their key properties involving CO 2 absorption rates and capacities, and in particular desorption temperature. [6][7][8][9][10][11] Piperazine (PZ), a cyclic secondary amine, has a working capacity of 0.90 mol CO 2 /mol greater than 0.43 mol CO 2 / mol of MEA. 12 The larger CO 2 -absorbing capacity of PZ than MEA is due to the fact that there are two potentially reactive secondary amine groups in PZ whereas MEA has only one. In addition, although PZ has more sterically congested reactive sites than MEA, it can absorb and desorb CO 2 much faster than MEA. 13 Accordingly, PZ is also regarded as one of the promising amine sorbents, and, in fact, is suggested as a main component of the KS-1 sorbent currently used in the established Mitsubishi process. 14 As an additive, PZ can play a role in promoting the absorption rate of others, e.g., sterically hindered 2-amino-2-methyl-1propanol (AMP) or even tertiary amines. 14,15 Because of these interesting properties, PZ has attracted great attention for their applications to various CO 2 absorption reactions. However, PZ involves many reaction pathways in aqueous solution, and on account of the complex chemistry the consensus on the reaction mechanisms has not been achieved thus far. 16 In this regard, herein our experimental results on the isolation of PZ-dicarbamate, and the elucidation of its crystal structure will contribute to further understanding of the PZ-involved CO 2 -absorption reactions.In aqueous solution, PZ involves successive protonation and CO 2 -absorption reactions ( Figure S1, Supporting Information). At 25 C, the first and second protonation constants of PZ are reported to be log K = 9.77 and 5.60 M −1 , respectively, 17 and thus protonated PZ (HPZ + ) is able to accept one more proton to give doubly protonated PZ (H 2 PZ 2+ ). The protons are released during the carbamate formation reaction; e.g., PZ reacts with CO 2 to give PZcarbamate (PZC − ), accompanied by a proton release to a base. The mono-protonated PZ (HPZ + ) still has a reactive site which can ...