The complexation of metal ions and amines can mediate the chemical equilibrium and the thermal effect between amines and CO 2 , thus promoting the absorption and desorption of CO 2 in amine absorbents. In this work, the effects of Cu(II) on the performances of CO 2 absorption and desorption in the Cu(II)− MMEA (2-(methylamino)ethanol)−H 2 O system were studied. The thermal desorption results show that the temperature increase during CO 2 absorption can be mitigated in the presence of Cu(II), and the desorption performance of CO 2 can be obviously improved at 75−95 °C. Using the thermal desorption at 85 °C, the CO 2 desorption efficiency of MMEA solution containing 0.1 M [Cu] is 16.4% higher than that without cupric ions, and the regeneration energy consumption is reduced by 25%. The electrochemical research results indicate that the electrode structure and temperature affect the electrolysis rate of anodic copper, and the temperature is the key factor to enhance the CO 2 desorption rate. Only considering the decomposition voltage, the energy consumption of the absorbent regeneration is 0.5 GJ/t CO 2 at 50 °C, which is much lower than that of the thermal desorption method. The anode current efficiency is always about 100%. Increasing the temperature can increase the cathode current efficiency. When nickel foam with a large specific surface area is used as the cathode, the current efficiency can be increased to 100% at 50 °C. The CO 2 desorption is significantly improved in a Cu(II)-assisted MMEA−H 2 O system. The electrochemical method can achieve a desired desorption at a relatively low temperature and greatly reduce the energy consumption of amine absorbent regeneration.