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首页> 外文期刊>Journal of Zhejiang University. Science, A >A novel application of the SAWD-Sabatier-SPE integrated system for CO2 removal and O2 regeneration in submarine cabins during prolonged voyages
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A novel application of the SAWD-Sabatier-SPE integrated system for CO2 removal and O2 regeneration in submarine cabins during prolonged voyages

机译:锯切 - Sabatier-SPE集成系统在长时间航行期间二氧化碳舱切除和O2再生的新型应用

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To improve the working and living environment of submarine crews, an integrated system of 2 removal%29&ck%5B%5D=abstract&ck%5B%5D=keyword'>CO2 removal and 2 regeneration%29&ck%5B%5D=abstract&ck%5B%5D=keyword'>o2 regeneration was designed to work under experimental conditions for 50 people in a submarine cabin during prolonged voyages. The integrated system comprises a solid amine water desorption (SAWD) unit for CO2 collection and concentration, a sabatier reactor for CO2 reduction and a solid polymer electrolyte (SPE) unit for 2 regeneration%29&ck%5B%5D=abstract&ck%5B%5D=keyword'>o2 regeneration by electrolysis. The performances of the SAWD-Sabatier-SPE integrated system were investigated. The experimental results from the SAWD unit showed that the average CO2 concentration in the CO2 storage tank was more than 96% and the outlet CO2 concentration was nearly zero in the first 45 min, and less than 1/10 of inlet CO2 after 60 min when input CO2 was 0.5% (1000 L). About 950 L of CO2 was recovered with a recovery rate of 92%~97%. The output CO2 concentration was less than 0.2%, which showed that the adsorption-desorption performance of this unit was excellent. In the CO2 reduction unit we investigated mainly the start-up and reaction performance of the sabatier reactor. The start-up time of the sabatier reactor was 6, 8 and 10 min when the start-up temperature was 187.3, 179.5 and 168 °C, respectively. The product water was colorless, transparent, and had a pH of 6.9~7.5, and an electrical conductivity of 80 μs/cm. The sum of the concentration of metal ions (Ru3+, Al3+, Pb2+) was 0.028% and that of nonmetal ions (Cl?, SO42?) was 0.05%. In the 2 regeneration%29&ck%5B%5D=abstract&ck%5B%5D=keyword'>o2 regeneration unit, the O2 generation rate was 0.48 m3/d and the quantity was 2400 L, sufficient to meet the submariners’ basic oxygen demands. These results may be useful as a basis for establishing CO2-level limits and 2 regeneration%29&ck%5B%5D=abstract&ck%5B%5D=keyword'>o2 regeneration systems in submarines or similar enclosed compartments during prolonged voyages.
机译:为了改善潜艇机组人员的工作和生活环境,综合系统2 removal %29&ck %5b %5d = abstract&ck %5b %5d = weleply'> co2 removal和2再生%29&ck %5b %5d =摘要&ck %5b %5d =关键词'> O2再生旨在在长时间航行期间在潜艇舱内的50人下工作。集成系统包括用于CO 2收集和浓度的固体胺水解吸(SAWD)单元,用于CO 2还原的驻扎式反应器和2个再生的固体聚合物电解质(SPE)单元%29&CK %5b %5d = abstract&ck % 5b %5d =关键字'> O2通过电解再生。研究了Sawd-Sabatier-SPE集成系统的性能。 Sawd单元的实验结果表明,CO 2储罐中的平均CO 2浓度大于96℃,出口CO2浓度在前45分钟内几乎为零,60分钟后的入口CO2小于1/10当输入CO2为0.5 %(1000L)时。回收约950μl的二氧化碳,回收率为92〜%〜97 %。输出CO2浓度小于0.2±%,表明该单位的吸附 - 解吸性能优异。在二氧化碳还原单元中,我们主要研究了塔巴达特反应器的启动和反应性能。当启动温度分别为187.3,179.5和168°C时,塔巴替炉反应器的启动时间为6,8和10分钟。产品水是无色的,透明的,具有6.9〜7.5的pH,电导率为80μs/ cm。金属离子浓度(Ru3 +,Al3 +,Pb2 +)的总和为0.028℃,非金属离子(Cl 3 SO 4 2 =)为0.05℃。在2再生%29&CK %5B %5D = Abstract&CK %5B %5d =关键词'> O2再生单元时,O2生成率为0.48m 3 / d,数量为2400升,足以满足潜艇器'基本氧气需求。这些结果可用作建立CO2级限制的基础和2个再生%29&CK %5B %5D = Abstract&CK %5B %5D =关键词“> O2再生系统在潜艇或类似封闭的隔间期间在潜艇期间。

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