Journal of Zhejiang University SCIENCE A
ISSN 1673-565X(Print), 1862-1775(Online), Monthly
2009 Vol. 10 No. 11 p. 1642~1650
On-line Access Date: Nov. 9, 2009A novel application of the SAWD-Sabatier-SPE integrated system for CO2 removal and O2 regeneration in submarine cabins during prolonged voyages
Zhi HUANG1, Zhao-bo CHEN†‡1, Nan-qi REN1, Dong-xue HU2, Dong-huan ZHENG1, Zhen-peng ZHANG3
(1State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150090, China)
(2School of Materials Science & Chemical Engineering, Harbin Engineering University, Harbin 150001, China)
(3Institute of Environmental Science and Engineering, Nanyang Technological University, 637723, Singapore)
‡ Corresponding Author
†E-mail: czbhdx@163.com
Received Apr. 8, 2009; revision accepted Aug. 10, 2009; Crosschecked Sept. 10, 2009
Abstract: To improve the working and living environment of submarine crews, an integrated system of CO2 removal and 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 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 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 O2 regeneration systems in submarines or similar enclosed compartments during prolonged voyages.
Key words: CO2 removal, O2 regeneration, Solid amine water desorption (SAWD), Sabatier reactor, Solid polymer electrolyte (SPE), Submarine
doi:10.1631/jzus.A0920017 CLC number: X703
References:
[1] Ai, S.K., Zhou, D., Sun, J.B., Hou, W.H., Zhou, K.H., 2000. A study of temperature catalyst for sabatier reaction. Space Medicine and Medical Engineering, 13(2):277-280.
[2] Araki, T., Taniuchi, T., Sunakawa, D., Nagahama, M., Onda, K., Kato, T., 2007. Cycle analysis of low and high H2 utilization SOFC/gas turbine combined cycle for CO2 recovery. Journal of Power Sources, 171(2):464-470.
[3] Chen, Z.W., Xu, W.G., Guan, Y.M., Zhang, Q., 2006. Basic theoretical analysis for CO2 removal in submarine atmosphere by solid amine. Chemical Defence in Ship, 28(4):86-87.
[4] Choi, P., Bessarabov, D.G., Datta, R., 2004. A simple model for solid polymer electrolyte (SPE) water electrolysis. Solid State Ionics, 175(1-4):535-539.
[5] Diaz, E., Munoz, E., Vega, A., Ordonez, S., 2008. Enhancement of the CO2 retention capacity of X zeolites by Na- and Cs-treatments. Chemosphere, 70(8):1375-1382.
[6] Gray, M.L., Champagne, K.J., Fauth, D., Baltrus, J.P., Pennline, H., 2008. Performance of immobilized tertiary amine solid sorbents for the capture of carbon dioxide. International Journal of Greenhouse Gas Control, 2(1):3-8.
[7] Keshavarz, P., Fathikalajahi, J., Ayatollahi, S., 2008. Analysis of CO2 separation and simulation of a partially wetted hollow fiber membrane contactor. Journal of Hazardous Materials, 152(3):1237-1247.
[8] Kunugi, A., Fujioka, M., Yasuzawa, M., Inaba, M., Ogumi, Z., 1998. Electroreduction of 2-cyclohexen-1-one on metal-solid polymer electrolyte composite electrodes. Electrochimica Acta, 44(4):653-657.
[9] Li, J., Ai, S.K., Zhou, K.H., 1999. An experimental study of the Sabatier CO2 reduction subsystem for space station. Space Medicine and Medical Engineering, 12(2): 121-124.
[10] Liu, J.X., Hou, W.H., 2004. Study on Ru-based catalyst used in reductive reaction of CO2. Space Medicine and Medical Engineering, 17(6):457-460.
[11] Meng, Y.Y., Shang, C.X., 1994. A study on CO2 methanization reduction technology. Space Medicine and Medical Engineering, 6-7(2):115-117.
[12] Millet, P., Andolfatto, F., Durand, R., 1995. Design and performance of a solid polymer electrolyte water electrolyzer. International Journal of Hydrogen Energy, 93:87-93.
[13] Mouritz, A.P., Gellert, E., Burchill, P., Challis, K., 2001. Review of advanced composite structures for naval ships and submarines. Composite Structures, 53(1):21-41.
[14] Otsuji, K., Sawada, T., Satoh, S., Kanda, S., Matsumura, H., Kondo, S., Otsubo, K., 1987. Preliminary experimental results of gas recycling subsystems except carbon dioxide concentration. Advances in Space Research, 7(4):69-72.
[15] Rasten, E., Hagen, G., Tunold, R., 2003. Electrocatalysis in water electrolysis with solid polymer electrolyte. Electrochimica Acta, 48(25-26):3945-3952.
[16] Ross, C.T.F., 2006. A conceptual design of an underwater vehicle. Ocean Engineering, 33(16):2087-2104.
[17] Russell, J.F., Klaus, D.M., 2007. Maintenance, reliability and policies for orbital space station life support systems. Reliability Engineering and System Safety, 92(6):808-820.
[18] Shen, L.P., Zhou, K.H., 2000. Testing of crew cabin air revitalization system in space station. Chinese Journal of Space Science, 10(20):57-76.
[19] Tanaka, Y., Uchinashi, S., Saihara, Y., Kikuchi, K., Okay, T., Ogumic, Z., 2003. Dissolution of hydrogen and the ratio of the dissolved hydrogen content to the produced hydrogen in electrolyzed water using SPE water electrolyzer. Electrochimica Acta, 48(27):4013-4019.
[20] Tanaka, Y., Kikuchi, K., Saihara, Y., Ogumic, Z., 2005. Bubble visualization and electrolyte dependency of dissolving hydrogen in electrolyzed water using Solid-Polymer-Electrolyte. Electrochimica Acta, 50(25-26):5229-5236.
[21] Tang, J.K., Ba, J.Z., Jiang, Y.X., Li, J., 2006. Review of solid polymer electrolyte water electrolysis. Chemical Defence on Ship, 3(20-25):20-21.
[22] Zhang, H.B., 2006. Submarine atmosphere pollution and detection technology. Chemical Defenses on Ships, 2:1-5.
[23] Zhang, J., Singh, R., Webley, P.A., 2008. Alkali and alkaline-earth cation exchanged chabazite zeolites for adsorption based CO2 capture. Microporous and Mesoporous Materials, 111(1-3):478-487.
[24] Zhang, Y.J., Wang, C., Wan, N.F., Liu, Z.X., Mao, Z.Q., 2007. Study on a novel manufacturing process of membrane electrode assemblies for solid polymer electrolyte water electrolysis. Electrochemistry Communications, 9(4):667 -670.
[25] Zhao, H.L., Hu, J., Wang, J.J., Zhou, L.H., Liu, H.L., 2007. CO2 capture by the amine-modified mesoporous materials. Acta Physico-Chimica Sinica, 23(6):801-806.
[26] Zhao, Y.S., 2001. Technology research of solid amine CO2 removal. Naval Vessel Science and Technology, 3:23-25.
[27] Zhou, K.H., Fu, L., Han, Y.Q., Li, J.R., 2003. Research and development of technology of regenerative environmental control and life support system. Space Medicine and Medical Engineering, 16(5):566-572.
[28] Zhou, K.H., Han, Y.Q., Wu, B.Z., Zhao, P.S., 2004. Testing result and analysis of a regenerable solid amine CO2 control system. Space Medicine and Medical Engineering, 17(4):287-291.
[29] Zhou, K.H., Yin, Y.L., Wang, F., 2007. The design and experiment of solid polymer electrolyte water electrolytic cell. Space Medicine and Medical Engineering, 20(6):427-431.