Removal of Hg0 with sodium chlorite solution and mass transfer reaction kinetics

2010 ◽  
Vol 53 (5) ◽  
pp. 1258-1265 ◽  
Author(s):  
Yi Zhao ◽  
SongTao Liu ◽  
Jie Yao ◽  
XiaoYing Ma ◽  
ChuanMin Chen
Author(s):  
Le Xie ◽  
Qi-An Wang ◽  
Xian-Jin Luo ◽  
Zheng-Hong Luo

Abstract Solid particle dispersion and chemical reactions in high-viscosity non-Newtonian fluid are commonly encountered in polymerization systems. In this study, an interphase mass transfer model and a finite-rate/eddy-dissipation formulation were integrated into a computational fluid dynamics model to simulate the dispersion behavior of particles and the mass transfer–reaction kinetics in a condensation polymerization-stirred tank reactor. Turbulence fields were obtained using the standard k–ε model and employed to calculate the mixing rate. Cross model was used to characterize the rheological property of the non-Newton fluid. The proposed model was first validated by experimental data in terms of input power. Then, several key operating variables (i.e. agitation speed, viscosity, and particle size) were investigated to evaluate the dispersive mixing performance of the stirred vessel. Simulation showed that a high agitation speed and a low fluid viscosity favored particle dispersions. This study provided useful guidelines for industrial-scale high-viscosity polymerization reactors.


Fuel ◽  
2013 ◽  
Vol 108 ◽  
pp. 254-260 ◽  
Author(s):  
Yangxian Liu ◽  
Jianfeng Pan ◽  
Aikun Tang ◽  
Qian Wang

RSC Advances ◽  
2017 ◽  
Vol 7 (31) ◽  
pp. 18821-18829 ◽  
Author(s):  
Zhitao Han ◽  
Shaolong Yang ◽  
Dongsheng Zhao ◽  
Bojun Liu ◽  
Xinxiang Pan ◽  
...  

The mass transfer-reaction kinetics of NO absorption by wet scrubbing using electrolyzed seawater was studied in a bench-scale bubbling reactor.


2012 ◽  
Vol 51 (37) ◽  
pp. 12065-12072 ◽  
Author(s):  
Yangxian Liu ◽  
Jianfeng Pan ◽  
Jun Zhang ◽  
Aikun Tang ◽  
Yong Liu

2014 ◽  
Vol 37 (10) ◽  
pp. 1797-1804 ◽  
Author(s):  
Hong Yin ◽  
Caiping Sheng ◽  
Zhirong Chen ◽  
Shenfeng Yuan ◽  
Haoran Li ◽  
...  

2019 ◽  
Vol 12 (11) ◽  
pp. 6193-6208 ◽  
Author(s):  
Rupert Holzinger ◽  
W. Joe F. Acton ◽  
William J. Bloss ◽  
Martin Breitenlechner ◽  
Leigh R. Crilley ◽  
...  

Abstract. In September 2017, we conducted a proton-transfer-reaction mass-spectrometry (PTR-MS) intercomparison campaign at the CESAR observatory, a rural site in the central Netherlands near the village of Cabauw. Nine research groups deployed a total of 11 instruments covering a wide range of instrument types and performance. We applied a new calibration method based on fast injection of a gas standard through a sample loop. This approach allows calibrations on timescales of seconds, and within a few minutes an automated sequence can be run allowing one to retrieve diagnostic parameters that indicate the performance status. We developed a method to retrieve the mass-dependent transmission from the fast calibrations, which is an essential characteristic of PTR-MS instruments, limiting the potential to calculate concentrations based on counting statistics and simple reaction kinetics in the reactor/drift tube. Our measurements show that PTR-MS instruments follow the simple reaction kinetics if operated in the standard range for pressures and temperature of the reaction chamber (i.e. 1–4 mbar, 30–120∘, respectively), as well as a reduced field strength E∕N in the range of 100–160 Td. If artefacts can be ruled out, it becomes possible to quantify the signals of uncalibrated organics with accuracies better than ±30 %. The simple reaction kinetics approach produces less accurate results at E∕N levels below 100 Td, because significant fractions of primary ions form water hydronium clusters. Deprotonation through reactive collisions of protonated organics with water molecules needs to be considered when the collision energy is a substantial fraction of the exoergicity of the proton transfer reaction and/or if protonated organics undergo many collisions with water molecules.


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