蒸馏
工艺工程
能源消耗
多效蒸馏
环境科学
废物管理
减压蒸馏
化学
工程类
色谱法
电气工程
作者
Shiwei Qiao,Min Xu,Xiaofei Lv,Huijun Zhao
标识
DOI:10.1002/ceat.202400296
摘要
Abstract Carbon capture utilization and storage‐enhanced oil recovery (EOR) is often considered the most promising technology for utilizing CO 2 . Cryogenic distillation is also viewed as the most reasonable separation option for handling CO 2 ‐EOR gases, despite being an energy‐intensive process. The main challenge for this technology is energy loss. To overcome this challenge, one potential alternative is to optimize the system processes and parameters. This study proposes a new process to reduce distillation energy consumption by refluxing the distillate back to the distillation column. Operational parameter optimization was performed using the commercial simulator Aspen HYSYS for modeling and sensitivity analysis of process parameters using orthogonal experimental methods. The simulation results indicate that after optimization, the energy consumption in the distillation process decreased from 0.207 to 0.196 MJ kg −1 , whereas the purity decreased slightly from 94.63 % to 94.52 %. However, the recovery increased from 97.8 % to 97.88 %, and the total energy consumption decreased from 0.772 to 0.761 MJ kg −1 .
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