Temperature and pressure dependence of the CO₂ absorption through a ceramic hollow fiber membrane contactor (CHFMC) modules were extensively evaluated and optimized. Results are presented for a CHFMC module consisting of 200 ceramic fibers in a single compact unit. The effect of gas temperatures and liquid absorbent temperatures was studied by altering the CO₂ gas (N₂ balance) and monoethanolamine (MEA) absorbent temperatures (20−50 °C). CO₂ removal efficiency (%) was also evaluated as a function of CO₂ gas composition (1.5–13 %, N₂ balance). The CO₂ removal efficiency (%) slightly increases when the temperature of the injected gas temperature increases from 20 °C to 40 °C, and then decreases as the temperature further increases from 40 °C to 50 °C. The MEA absorbent temperatures did not have a notable effect on the CHFMC module performance in the specific temperature range studied in this work. The effects of the liquid pressure drop do not appear to be significant for a given gas flow rate, but the gas pressure drop increases with gas flow rate and gas temperature. The findings in this study show that a CHFMC process is affected by the CO₂ gas temperature and composition but quite independent of the MEA absorbent temperature.

广泛评估和优化了通过陶瓷中空纤维膜接触器（CHFMC）模块吸收CO _2的温度和压力依赖性。给出了一个紧凑的单元中由200根陶瓷纤维组成的CHFMC模块的结果。通过改变CO ₂气体（N ₂平衡）和单乙醇胺（MEA）吸收剂温度（20-50°C）来研究气体温度和液体吸收剂温度的影响。还评估了CO ₂去除效率（％）与CO ₂气体成分（1.5-13％，N ₂平衡）的关系。一氧化碳₂当注入气体温度从20°C升高到40°C时，去除效率（％）略有增加，然后随着温度从40°C进一步升高到50°C而降低。在这项工作研究的特定温度范围内，MEA吸收剂温度对CHFMC组件的性能没有显着影响。对于给定的气体流速，液体压降的影响似乎并不明显，但是气体压降随气体流速和气体温度的增加而增加。这项研究的结果表明，CHFMC过程受CO ₂气体温度和组成的影响，但与MEA吸收剂温度完全无关。