Jian-Gang Lu
Nanjing University of Information Science and Technology
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Featured researches published by Jian-Gang Lu.
Separation Science and Technology | 2010
Jian-Gang Lu; Yan Ji; Hui Zhang; Mindong Chen
An activated solution based on amino acid salt was proposed as a CO2 absorbent. Piperazine (PZ) was selected as an activating agent and added into the aqueous glycine salt to form the activated solution. A coupling process, which associated the activated solution with a PP hollow fiber membrane contactor, was set up. An experimental and theoretical analysis for CO2 capture was performed. The performances of CO2 capture by the coupling process were evaluated using the PZ activated solution and the non-activated glycine salt solution. A numerical model for the simulation of the hollow fiber membrane gas–liquid mass transfer was developed. Typical parameters such as outlet gas phase CO2 concentration, capture efficiency, and mass transfer coefficient for the activated solution were determined experimentally. The effects of operation temperature and liquid CO2-loading on mass transfer coefficient and capture efficiency were discussed in this work. Axial and radial concentration profiles of CO2 in the fiber lumen and mass transfer flux were simulated by the model. Results show that the performances of the PZ activated glycine salt solution are evidently better than that of the non-activated glycine salt solution in the membrane contactor for CO2 capture. Elevation of the operation temperatures can enhance the overall mass transfer coefficient. The activated solution can maintain higher capture efficiency especially in the case of high CO2-loadings. The gas phase CO2 concentration with the activated solution is lower than that with the non-activated solution whether along axial or radial distances in the fiber lumen. The model simulation is validated with experimental data.
Journal of Chemistry | 2014
Zhengwen Xu; Yunlong Zhao; Jing Shi; Jian-Gang Lu; Ling Cheng; Mindong Chen
As new emerging pollutants, phthalic acid monoesters (PAMs) pose potential ecological and human health risks. In the present study, adsorption performance of monobutyl phthalate (MBP) onto two macroporous base anion-exchange resins (D-201 and D-301) was discussed. It was found that the adsorption isotherms were best fitted by the Langmuir equation while the adsorption kinetics were well described by pseudo-first-order model. Analyses of sorption isotherms and thermodynamics proved that the adsorption mechanisms for DBP onto D-201 were ion exchange. However, the obtained enthalpy values indicate that the sorption process of MBP onto D-301 is physical adsorption. The equilibrium adsorption capacities and adsorption rates of DBP on two different resins increased with the increasing temperature of the solution. D-301 exhibited a higher adsorption capacity of MBP than D-201. These results proved that D-301, as an effective sorbent, can be used to remove phthalic acid monoesters from aqueous solution.
International Journal of Chemical Reactor Engineering | 2011
Jian-Gang Lu; Fan Fan; Cong Liu; Yan Ji; Hui Zhang
A novel composite solution consisting of N-methylmonoethanolamine (MM-EA) and 2-amino-2-methyl-1-propanol (AMP) as a CO2 absorbent was proposed. Coupling process of membrane contactor and the composite solution was investigated. The performance of the coupling was experimentally compared between the single and composite solution. Overall mass transfer coefficients were determined. Effects of various factors, such as flow rates and operation temperatures on mass transfer of membrane contactor, were studied. Comparison of prediction for overall mass transfer coefficients using a resistance in series model with experimental values was performed. Results show that performance of the composite solution is evidently better than that of the single MMEA solution. The overall mass transfer coefficient with the composite solution is much higher than that with the single MMEA solution. Higher operation temperature can enhance mass transfer of membrane contactor. Operation parameters such as flow rates can promote mass transfer, but the promotion is limited. Enhance of mass transfer relies essentially on chemical reaction. Model values are in good agreement with experimental ones.
Journal of Membrane Science | 2008
Jian-Gang Lu; You-Fei Zheng; Min-Dong Cheng
Separation and Purification Technology | 2006
Jian-Gang Lu; You-Fei Zheng; Du-Liang He
Journal of Membrane Science | 2007
Jian-Gang Lu; You-Fei Zheng; Min-Dong Cheng; Lianjun Wang
Applied Energy | 2014
Jian-Gang Lu; Chun-Ting Lu; Yue Chen; Liu Gao; Xin Zhao; Hui Zhang; Zhengwen Xu
Desalination | 2009
Jian-Gang Lu; You-Fei Zheng; Min-Dong Cheng
Journal of Chemical & Engineering Data | 2011
Jian-Gang Lu; Fan Fan; Cong Liu; Hui Zhang; Yan Ji; Mindong Chen
Journal of Molecular Liquids | 2015
Jian-Gang Lu; Zhen-Yu Lu; Liu Gao; Shuang Cao; Jia-Ting Wang; Xiang Gao; Yin-Qin Tang; Wen-Yi Tan