PROJECT MISTT: MESOSCALE PLUME MODELING OF THE DISPERSION, TRANSFORMATION AND GROUND REMOVAL OF SO2

1978 ◽  
pp. 569-588 ◽  
Author(s):  
N.V. GILLANI
2005 ◽  
Vol 20 (1-2) ◽  
pp. 119-125 ◽  
Author(s):  
Chris Kennedy ◽  
Hans Ericsson ◽  
P. L. R. Wong

Author(s):  
Shuo Li ◽  
M. R. Flynn

AbstractVisible plumes above wet cooling towers are of great concern due to the associated aesthetic and environmental impacts. The parallel path wet/dry cooling tower is one of the most commonly used approaches for plume abatement, however, the associated capital cost is usually high due to the addition of the dry coils. Recently, passive technologies, which make use of free solar energy or the latent heat of the hot, moist air rising through the cooling tower fill, have been proposed to minimize or abate the visible plume and/or conserve water. In this review, we contrast established versus novel technologies and give a perspective on the relative merits and demerits of each. Of course, no assessment of the severity of a visible plume can be made without first understanding its atmospheric trajectory. To this end, numerous attempts, being either theoretical or numerical or experimental, have been proposed to predict plume behavior in atmospheres that are either uniform versus density-stratified or still versus windy (whether highly-turbulent or not). Problems of particular interests are plume rise/deflection, condensation and drift deposition, the latter consideration being a concern of public health due to the possible transport and spread of Legionella bacteria.


Author(s):  
Patricia Luis ◽  
Inmaculada Ortiz ◽  
Rubén Aldaco ◽  
Aurora Garea ◽  
Ángel Irabien

Removal of SO2 from gas emissions by selective absorption into a liquid is a common method to reduce air pollution and environmental risks. The absorption efficiency is determined by the interaction between the gases and the liquid. A great number of gas desulphurization methods have been developed where aqueous or organic solvents are used as sorbents.N,N-dimethylaniline (DMA) is an organic solvent used in the industry because its affinity with SO2. This absorption is neither too strong nor too weak, thus absorption and desorption can occur leading to a regenerative process where SO2 can be recovered. However, a direct contact between SO2 and DMA leads to several environmental problems caused by solvent evaporation and drops dragging into the gas stream.In order to increase the process efficiency and reduce environmental risks, a non-dispersive absorption process using hollow fibre membrane modules is developed in this work for a solvent zero emission process. The mass transfer into a fibre may be described by three main assumptions: gas-phase laminar flow, gas-phase plug-flow and gas-phase mixing. A numerical calculation was carried out to establish the performance of a hollow fibre membrane contactor for the removal of SO2 when water and N,N-dimethylaniline are used as sorbents in order to compare both, wetted and non-wetted operating modes.


2011 ◽  
Vol 241 (5) ◽  
pp. 1667-1700 ◽  
Author(s):  
Timothy L. Norman ◽  
Shripad T. Revankar

2014 ◽  
Vol 29 (1) ◽  
pp. 377-383 ◽  
Author(s):  
Yanran Zuo ◽  
Honghong Yi ◽  
Xiaolong Tang

1993 ◽  
Vol 119 (3) ◽  
pp. 414-423 ◽  
Author(s):  
Moo Been Chang ◽  
Mark J. Kushner ◽  
Mark J. Rood
Keyword(s):  

2014 ◽  
Vol 240 ◽  
pp. 462-468 ◽  
Author(s):  
Ritesh Tailor ◽  
Asieh Ahmadalinezhad ◽  
Abdelhamid Sayari

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