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121.
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该文对多个完全混合流釜式反应器的优化组合进行了探讨,得出了使总容积为最小的各反应器出口转化率计算的递推公式,为反应器组合的研究和工业装置的优化排列提供了参考。 相似文献
123.
采用有限元分析软件ANSYS,对天然气水合物反应釜进行了应力计算和分析。在保证其它要求的情况下,以重量最小为优化目标,对其重要尺寸进行了优化设计和计算,得到了最合理的尺寸,达到减小容器总质量、降低成本的目的。这对水合物法储运天然气具有重要意义。 相似文献
124.
综合讨论了厌氧折流板反应器(ABR)工艺特征,阐述了国内外关于ABR启动及实际应用的研究现状。认为ABR具有耐冲击负荷、对有毒物质适应性强、固液分离效果好等显著特点。因此,ABR作为一种新型高效生物处理技术,在我国废水处理中,特别是对高浓度有毒工业废水处理具有良好的研究开发价值。 相似文献
125.
DEHGHANI Mohammad Hadi MAHVI Amir Hossein NAJAFPOOR Ali Asghar AZAM Kamal 《浙江大学学报(A卷英文版)》2007,8(9):1462-1468
The effectiveness of using acoustical (sonochemical) reactor for degradation of linear alkylbenzen sulfonate (LAS) from aqueous solution was investigated. LASs are anionic surfactants,found in relatively high amounts in domestic and industrial wastewaters. In this study,experiments on LAS solution were performed using methylene blue active substances (MBAS) method. The effectiveness of acoustical processor reactor for LAS degradation is evaluated with emphasis on the effect of treatment time and initial LAS concentration. Experiments were performed at initial concentrations of 0.2,0.5,0.8 and 1.0 mg/L,acoustic fre-quency of 130 kHz,applied power of 500 W and temperature of 18 °C~20 °C. At the conditions involved,LAS degradation was found to increase with increasing sonochemical time. In addition,as the concentration increased,the LAS degradation rate de-creased in the acoustical processor reactor. 相似文献
126.
马俊林 《十堰职业技术学院学报》2000,13(2):10-15
探讨了环管反应器中高粘度催化剂的混合特征,研究了液体循环速率、催化剂粘度对混合过程的影响,并对混合过程进行了观察分析,建立了该过程的教学模型,模型值和实验值吻合较好。 相似文献
127.
崔迎 《天津职业院校联合学报》2010,12(5):3-5
催化湿式氧化是针对高浓度难降解有机工业废水处理而开发的一项高级氧化技术.研究具有应用前景的滴流床反应器的特征、参数和在催化湿式氧化中的作用,为工业废水的催化湿式氧化处理的实际应用奠定了基础. 相似文献
128.
研制了一种新型数控立式绕线机用于并联空心电抗器的制造,具有自动绕线、倒线、浸胶、缠纱等多种功能。现场使用情况表明:该绕线机操作、维护方便,工作可靠,自动化程度高,其绕线和缠纱精度、生产效率比普通立式绕线机有很大提高。 相似文献
129.
Zhi Huang Zhao-bo Chen Nan-qi Ren Dong-xue Hu Dong-huan Zheng Zhen-peng Zhang 《浙江大学学报(A卷英文版)》2009,10(11):1642-1650
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. 相似文献
130.