Abstract
Methanol synthesis, a crucial platform chemical and clean energy carrier, plays a significant role in the global energy transition. This study focuses on thermodynamic optimization and carbon cycle intensification of the CO/CO(2) hydrogenation process. A multidimensional reaction system model was developed to investigate the effects of the CO/CO(2) feed ratio, H(2)/CO (x) molar ratio, reaction temperature and pressure, catalyst efficiency, and gas-liquid mass transfer resistance on product distribution. To improve carbon utilization, an innovative steam stripping-coupled cycle process was proposed, enabling efficient recovery of dissolved CO(2) in the liquid phase through phase equilibrium regulation. This reduced the CO(2) content from 10.72 kmol·h(-1) before stripping to 1.69 × 10(-4) kmol·h(-1) after stripping. Under optimized operating conditions, the methanol yield reached 82.0%, and the single-pass yields of CO and CO(2) were 90.7% and 72.6%, respectively. After the novel stripping cycle was adopted, the loss of liquid-phase CO(2) became negligible, with carbon and hydrogen losses mainly caused by gas-phase relaxation. When the relaxation rate was set to 1.0%, the utilization of CO (x) and H(2) reached 93.2% and 82.8%, respectively. This strategy established a dynamic reaction-separation-recycle balance, improving both resource efficiency and economic performance, and offering theoretical and technical guidance for green methanol industrialization.