To improve the working and living environment of submarine crews, an integrated system of CO 2 removal and O 2 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 CO 2 collection and concentration, a Sabatier reactor for CO 2 reduction and a solid polymer electrolyte (SPE) unit for O 2 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 CO 2 concentration in the CO 2 storage tank was more than 96% and the outlet CO 2 concentration was nearly zero in the first 45 min, and less than 1/10 of inlet CO 2 after 60 min when input CO 2 was 0.5% (1000 L). About 950 L of CO 2 was recovered with a recovery rate of 92%∼97%. The output CO 2 concentration was less than 0.2%, which showed that the adsorption-desorption performance of this unit was excellent. In the CO 2 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 (Ru 3+ , Al 3+ , Pb 2+ ) was 0.028% and that of nonmetal ions (Cl − , SO 4 2− ) was 0.05%. In the O 2 regeneration unit, the O 2 generation rate was 0.48 m 3 /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 CO 2 -level limits and O 2 regeneration systems in submarines or similar enclosed compartments during prolonged voyages.
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Huang et al. (2009) studied this question.
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