Gupta Mayuri, da Silva Eirik Falck, Svendsen Hallvard F
Department of Chemical Engineering, Norwegian University of Science and Technology, Sem Sælands vei 4, Trondheim 7491, Norway.
Department of Process Technology, SINTEF Industry, Trondheim 7034, Norway.
J Phys Chem B. 2022 Mar 10;126(9):1980-1991. doi: 10.1021/acs.jpcb.1c10755. Epub 2022 Feb 28.
Temperature-dependent correlations for equilibrium constants (ln ) and heat of absorption (Δ) of different reactions (i.e., deprotonation, double deprotonation, carbamate formation, protonated carbamate formation, dicarbamate formation) involved in the piperazine (PZ)/CO/HO system have been calculated using computational chemistry based ln values input to the Gibbs-Helmholtz equation. This work also presents an extensive study of gaseous phase free energy and enthalpy for different reactions using composite (G3MP2B3, G3MP2, CBS-QB3, and G4MP2) and density functional theory [B3LYP/6-311++G(d,p)] methods. The explicit solvation shell (ESS) model and SM8T solvation free energy coupled with gaseous phase density functional theory calculations give temperature-dependent reaction equilibrium constants for different reactions. Calculated individual and overall reaction equilibrium constants and enthalpies of different reactions involved in CO absorption in piperazine solution are compared against experimental data, where available, in the temperature range 273.15-373 K. Postcombustion CO capture (PCC) is a temperature swing absorption-desorption process. The enthalpy of the solution directly correlates with the steam requirement of the amine regeneration step. Temperature-dependent correlations for ln and Δ calculated using computational chemistry tools can help evaluate potential PCC solvents' thermodynamics and cost-efficiency. These correlations can also be employed in thermodynamic models (e.g., e-UNIQUAC, e-NRTL) to better understand postcombustion CO capture solvent chemistry.
利用输入吉布斯 - 亥姆霍兹方程的基于计算化学的ln 值,计算了哌嗪(PZ)/CO₂/H₂O体系中不同反应(即去质子化、双去质子化、氨基甲酸盐形成、质子化氨基甲酸盐形成、二氨基甲酸盐形成)的平衡常数(ln )与吸收热(Δ)的温度相关关系。这项工作还使用复合方法(G3MP2B3、G3MP2、CBS - QB3和G4MP2)以及密度泛函理论[B3LYP/6 - 311++G(d,p)]方法,对不同反应的气相自由能和焓进行了广泛研究。显式溶剂化壳(ESS)模型和SM8T溶剂化自由能与气相密度泛函理论计算相结合,给出了不同反应的温度相关反应平衡常数。将计算得到的哌嗪溶液中CO₂吸收涉及的不同反应的单个和整体反应平衡常数及焓与273.15 - 373 K温度范围内可得的实验数据进行了比较。燃烧后CO₂捕集(PCC)是一个变温吸收 - 解吸过程。溶液的焓与胺再生步骤的蒸汽需求直接相关。使用计算化学工具计算得到的ln 和Δ的温度相关关系有助于评估潜在PCC溶剂的热力学和成本效益。这些关系还可用于热力学模型(如e - UNIQUAC、e - NRTL),以更好地理解燃烧后CO₂捕集溶剂化学。