TY - JOUR
T1 - A Novel Coal-Based Calcium Carbide-Acetylene System Process Based on Multistage Carbon Capture and Waste Slag Recycling Design
T2 - A Multiobjective Optimization Evaluation Perspective
AU - Wang, Hongxia
AU - Zhu, Pengfei
AU - Dai, Min
AU - Wu, Xiaomei
AU - Yang, Fusheng
AU - Zhang, Zaoxiao
N1 - Publisher Copyright:
© 2022 American Chemical Society.
PY - 2023/1/11
Y1 - 2023/1/11
N2 - Large amounts of raw material consumption, high energy consumption, and severe pollution have always been the key factors restricting the stable development of the coal-to-calcium carbide industry. Therefore, this paper presents a novel combined carbon capture and utilization and solid waste recycling system of the coal-based calcium carbide-acetylene production (CCAP) process to improve these deficiencies. This improved CCAP system consists of a gasifier, carbide furnace, acetylene furnace, the newly designed coupling module of a recarbonization furnace and calciner, and mineralization units. The thermodynamic model of the CCAP system is developed to calculate the effective atomic yield, carbon consumption, CO2 emission, etc. to evaluate the performance. The improved system performed better with the effective atomic yield (98.50%), CO2 capture rate (69.57%), CO2 emission (1.1064 t CO2·(t-1C2H2)), CO2e emission (7.2092 t CO2e·(t-1C2H2)), and carbon consumption (3.2101 t Coal·(t-1C2H2)) than the referenced system with 64.57%, 0, 2.25 t CO2·(t-1C2H2), 20.4122 t CO2e·(t-1C2H2), and 5.43 t Coal·(t-1C2H2), respectively. The exergy analysis shows that the improved system performed better for efficient energy utilization with an exergy efficiency of 48.97% for a large-scale chemical process. Besides, the trade-off between the maximum effective atomic yield, minimum carbon consumption, CO2 equivalent emission, and total annual cost (TAC) is conducted through multiobjective optimization. By three-objective optimization, the improved system could achieve a lower TAC of 8.51 × 106 $/year, CO2e emission of 4.1573 t CO2e·(t-1C2H2), and carbon consumption of 1.9874 t Coal·(t-1C2H2) simultaneously, which decreased by 38.78%, 79.63%, and 63.40%, respectively, than that of the referenced system. The all-around performance of the improved CCAP system after multiobjective optimization has been dramatically improved, making it more competitive in energy conservation, emission reduction, and resource recovery.
AB - Large amounts of raw material consumption, high energy consumption, and severe pollution have always been the key factors restricting the stable development of the coal-to-calcium carbide industry. Therefore, this paper presents a novel combined carbon capture and utilization and solid waste recycling system of the coal-based calcium carbide-acetylene production (CCAP) process to improve these deficiencies. This improved CCAP system consists of a gasifier, carbide furnace, acetylene furnace, the newly designed coupling module of a recarbonization furnace and calciner, and mineralization units. The thermodynamic model of the CCAP system is developed to calculate the effective atomic yield, carbon consumption, CO2 emission, etc. to evaluate the performance. The improved system performed better with the effective atomic yield (98.50%), CO2 capture rate (69.57%), CO2 emission (1.1064 t CO2·(t-1C2H2)), CO2e emission (7.2092 t CO2e·(t-1C2H2)), and carbon consumption (3.2101 t Coal·(t-1C2H2)) than the referenced system with 64.57%, 0, 2.25 t CO2·(t-1C2H2), 20.4122 t CO2e·(t-1C2H2), and 5.43 t Coal·(t-1C2H2), respectively. The exergy analysis shows that the improved system performed better for efficient energy utilization with an exergy efficiency of 48.97% for a large-scale chemical process. Besides, the trade-off between the maximum effective atomic yield, minimum carbon consumption, CO2 equivalent emission, and total annual cost (TAC) is conducted through multiobjective optimization. By three-objective optimization, the improved system could achieve a lower TAC of 8.51 × 106 $/year, CO2e emission of 4.1573 t CO2e·(t-1C2H2), and carbon consumption of 1.9874 t Coal·(t-1C2H2) simultaneously, which decreased by 38.78%, 79.63%, and 63.40%, respectively, than that of the referenced system. The all-around performance of the improved CCAP system after multiobjective optimization has been dramatically improved, making it more competitive in energy conservation, emission reduction, and resource recovery.
UR - https://www.scopus.com/pages/publications/85145271369
U2 - 10.1021/acs.iecr.2c03947
DO - 10.1021/acs.iecr.2c03947
M3 - 文章
AN - SCOPUS:85145271369
SN - 0888-5885
VL - 62
SP - 571
EP - 585
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 1
ER -
