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多种形式可再生能源集成互补供暖供冷系统在农村地区的应用 被引量:6
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作者 孟祥德 邱松伟 《太阳能》 2010年第3期19-21,共3页
介绍了三种可在农村地区利用的可再生能源状况,提出了一种利用地热能、太阳能、生物质能三种形式可再生能源集成互补供暖供冷系统,并对此系统进行简要的热力学分析。
关键词 农村 再生能源 多种形式可再生能源集成互补供暖供冷系统 热力学分析
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聚酯片碎屑的自动化再生
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作者 王锌 《橡塑资源利用》 2005年第1期31-31,共1页
关键词 聚酯 自动化生产系统 集成再生系统 原料 回收技术
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采用分布式废水再生循环的塑料厂水系统集成
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作者 常凯亮 冯霄 王黎 《计算机与应用化学》 CAS 2016年第9期979-982,共4页
在水系统集成技术中,可以采用废水直接回用、再生回用和再生循环三种方式对用水网络进行优化。其中,再生循环用水网络可以最大限度地节约新鲜水消耗和减少废水的排放。废水再生单元可以是集中式或者分布式两种类型,本文对集中式和分布... 在水系统集成技术中,可以采用废水直接回用、再生回用和再生循环三种方式对用水网络进行优化。其中,再生循环用水网络可以最大限度地节约新鲜水消耗和减少废水的排放。废水再生单元可以是集中式或者分布式两种类型,本文对集中式和分布式两种类型的再生单元的特点及适用场合进行了讨论,并给出初步的选用原则。利用水系统集成技术对某塑料厂的现行用水网络进行优化,结合生产实际选用分布式再生单元对排放废水进行再生处理,优化后的塑料厂用水网络使高品质脱盐水的节水率达到70%。 展开更多
关键词 再生系统集成 循环 分布式 塑料厂
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A novel application of the SAWD-Sabatier-SPE integrated system for CO_2 removal and O_2 regeneration in submarine cabins during prolonged voyages 被引量:3
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作者 Zhi HUANG Zhao-bo CHEN +3 位作者 Nan-qi REN Dong-xue HU Dong-huan ZHENG Zhen-peng ZHANG 《Journal of Zhejiang University-Science A(Applied Physics & Engineering)》 SCIE EI CAS CSCD 2009年第11期1642-1650,共9页
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 pr... 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 rain when the start-up temperature was 187.3, 179.5 and 168 ℃, respectively. The product water was colorless, transparent, and had a pH of 6.9-7.5, and an electrical conductivity of 80μs/cm. The sum of the concentration of metal ions (Ru^3+, Al^3+, Pb^2+) was 0.028% and that of nonmetal ions (Cl^-, SO4^2-) was 0.05%. In the O2 regeneration unit, the O2 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 CO2-1evel limits and O2 regeneration systems in submarines or similar enclosed compartments during prolonged voyages. 展开更多
关键词 CO2 removal O2 regeneration Solid amine water desorption (SAWD) Sabatier reactor Solid polymer electrolyte (SPE) SUBMARINE
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