减轻载体饱和的便利运输膜脱碳稀释二氧化碳源:一个实验和技术经济研究

IF 4.9 Q1 ENGINEERING, CHEMICAL
Yang Han , W.S. Winston Ho
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引用次数: 5

摘要

以氨基酸盐为移动载体的催化运输膜(FTMs)在CO2浓度为0.05 ~ 20%的稀释原料气条件下,对其CO2/N2分离性能进行了表征。当CO2分压降低时,FTMs中的载流子饱和度降低,从而提高了CO2渗透率和CO2/N2选择性。含2-(1-哌嗪基)乙胺肌氨酸盐的最佳FTM的CO2渗透率从1968 ~ 3822 GPU上升,CO2/N2选择性从249 ~ 472提高,CO2含量从1%降至0.1%。通过设计一个两级富集膜级,进一步去除含CO2 1.75%的残余煤烟气中90%的CO2,验证了该FTM的可行性。技术经济分析表明,捕集成本较低,为每吨83.8美元。还对各种残余烟道气体超过90%捕获量的边际成本进行了评估,表明基于ftm的燃煤或水泥厂残余烟道气体捕获比直接空气捕获更具成本效益。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Mitigated carrier saturation of facilitated transport membranes for decarbonizing dilute CO2 sources: An experimental and techno-economic study

Mitigated carrier saturation of facilitated transport membranes for decarbonizing dilute CO2 sources: An experimental and techno-economic study

The CO2/N2 separation performances of facilitated transport membranes (FTMs) containing aminoacid salts as mobile carriers were characterized under dilute feed gases with 0.05–20% CO2. At a reduced CO2 partial pressure, the carrier saturation in the FTMs was mitigated, which enhanced both the CO2 permeance and CO2/N2 selectivity. The best FTM containing 2-(1-piperazinyl)ethylamine sarcosinate exhibited an uprising CO2 permeance from 1968 to 3822 GPU and an improved CO2/N2 selectivity from 249 to 472 with reducing CO2 content from 1% to 0.1%. The feasibility of this FTM is exemplified by designing a two-stage enriching membrane cascade to further remove 90% of the CO2 in a residual coal flue gas containing 1.75% CO2. Techno-economic analysis indicates a low capture cost of $83.8/tonne. The marginal costs beyond 90% capture are also evaluated for a variety of residual flue gases, indicating that the FTM-based capture from the coal or cement plant residual flue gas is more cost effective than direct air capture.

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