In the momentum of reducing the CO2 emission of coal to ethylene glycol (CtEG) process, a novel
carbon dioxide utilized coal to ethylene glycol (CUCtEG) process is
proposed, simulated, and optimized to find the optimal way for simultaneous
reduction and utilization of CO2 emissions of conventional
coal to ethylene glycol process. The novel process is integrated with
coke oven gas and dry/steam-mixed methane reforming technologies to
enhance resource and energy efficiencies as well as reduce CO2 emission. On the basis of the rigorous steady-state simulation
of the process, the key operational parameters of the proposed process
are investigated and optimized. A detailed technoeconomic analysis
is conducted to manifest the advantages of the proposed process by
comparison with a conventional process. The results show that the
optimal feed ratio of coke oven gas to coal is 0.68, and the split
ratio of CH4 for steam methane reforming reaction is suggested
to be 0.74. Compared with the conventional coal to ethylene glycol
process, the direct CO2 emission of the proposed process
is significantly reduced by 94.05%, and the carbon utilization efficiency
and exergy efficiency are greatly increased by 36.4% and 15.17%. Moreover,
the proposed process has a better economic performance and stronger
competitiveness since it can save the production cost by 9.72% and
improve the internal rate of return by 6.92%. Thus, the proposed process
provides a promising way to efficient utilization of CO2 and improve the technoeconomic performance of coal to ethylene glycol
industry.