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陈建孟, 蒲凤莲, 陈效, 孙永强
环境污染治理技术与设备,2004,1(5):61~64,-0001,():
-1年11月30日
汽油添加剂甲基叔丁基醚(MTBE)的污染在国外已引起重视。概述了目前MTBE生物降解的研究现状,着重介绍了国外对MTBE污染地下水的异位和原位生物处理方法。随着汽车的逐步普及和MTBE用量的增加,我国正在或将面临MTBE的污染。指出了开展相关研究的重要性和迫切性,初步提出了这一新课题的研究思路,为我国环境保护领域从事该项研究的人员提供参考。
甲基叔丁基醚 生物降解 植物修复
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陈建孟, 谭天恩, 史小农
高校化学工程学报,1995,2(9):142~148,-0001,():
-1年11月30日
以液滴离开塔板的初始位置为边缘分布、液滴粒径为条件分布。用概率统计的方法来描述旋流塔板上液滴群运动的边界条件.进而提出其三维模型。该模型不含可调参数,采用四阶Runge-Kutta法计算,结果得到实验的支持。
旋流塔板 运动模型 数值计算
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117浏览
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陈建孟, 王家德, 于建明
China Environmental Science. 2001, 21 (6): 503~506,-0001,():
-1年11月30日
通过驯化、筛选和富集培养,从制药厂(Y)和农药厂(N)生化曝气池的活性污泥中分离到2株能以二氯甲烷为唯一碳源和能源而生长的菌株。菌种初步鉴定为假单胞杆菌属和放线菌科分枝杆菌属。由正交试验得出GD11、GD23两株菌的最适培养条件:GD11温度28.5℃,pH值6.0,纱布层数6;GD23温度25℃,pH值7.2,纱布层数4。研究发现NaCl浓度对菌株的降解率有不同程度的抑制作用。
二氯甲烷, 生物降解
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陈建孟, Jianmeng Chen, *, Jiade Wang and Jianfeng Ma
J Chem Technol Biotechnol 81: 812-816 (2006),-0001,():
-1年11月30日
The effects of inlet gas concentration and gas flow-rate on the NO elimination process were studied in a laboratory-scale biofilter and the removal process is discussed. Various pollutant inlet concentrations and gas flow-rates were tested in the biofilter. The results showed that the removal efficiency increased with increase in the empty bed residence time (EBRT) and finally reached a steady state. The mass transfer process became the limiting step of NO removal when the EBRT was less than 2min. A removal efficiency of~73% was obtained in the biofilter at an inlet concentration of 107.1mgm−3. The removal efficiency decreased with increase in inlet concentration, whereas the removal capacity increased. The removal process consisted of chemical oxidation and bio-nitrification in the biofilter. The bioprocess mainly contributed to the removal.
biofiltration, nitric oxide, nitrification, air pollution
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陈建孟, 谭天恩, 史小农
化工学报,2003,12:1755~1760,-0001,():
-1年11月30日
Based on the results of gas flow field, droplet size distribution and droplet initial flow rate distribution on aф300mm rotating stream tray (RST), a three dimensional droplet projection trajectory model and a mass transfer efficiency model were developed. The calculation of the models was carried out by using a finite-difference procedure1 The predicted results of the plate efficiency agreed quite well with the experimental data measured with absorbing NH3 or SO2 on aф300mm RST and the operation data from a commercial ф3600mm RST column1 Meanwhile, the effect of gas-liquid system and RST's structure on plate efficiency was discussed.
旋流塔板 塔板效率 液滴抛射运动模型
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88浏览
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