摘要
An advanced cryogenic air separation process for oxy-combustion is proposed, based on self-heat recuperation technology. In contrast to double columns in the conventional cryogenic air separation process, a single distillation column only is used in the proposed process. By using self-heat recuperation technology, the heat of N-2 product gas from the top of the single distillation column is recirculated by exchanging heat with the liquid O-2 in the bottom and feed streams, largely reducing the energy requirement. The simulation results showed that the energy requirement of the proposed cryogenic air separation process was reduced by 20.2% compared with the conventional process when producing O-2 with low purity (95 mol%). The influence of compressor efficiency, minimum temperature difference in the main condenser and the O-2 product purity on the energy requirement were also investigated.
- 出版日期2016-1-15