scholarly journals FLUE GASES CLEANING FROM NITROGEN OXIDES BY ADDITIONAL OXIDATION OF NO TO NO2 AND ABSORPTION

2020 ◽  
Vol 42 (1) ◽  
pp. 77-85
Author(s):  
O.I. Sigal ◽  
D.Yu. Paderno

Experimental researches of operational characteristics of laboratory samples of two types of packing for the direct contact heat exchanger have been carried out, - Raschig ceramic rings and the developed construction with using the ribbon of amorphous metal alloy. The metal alloy packing slightly surpasses the ceramic one by the basic operational heat engineering parameters, and contributes to oxidation of the NO to water-soluble NO2, which enables to remove more of the latter by absorption with water and, as a result, to reduce the emissions of nitrogen oxides to the environment after contact apparatus by 35 % more efficiently than with using the ceramic packing.

1991 ◽  
Vol 40-41 ◽  
pp. 339-344 ◽  
Author(s):  
Elena D. Tabachnikova ◽  
E.B. Korolkova ◽  
Pavel Diko ◽  
J. Miskuf ◽  
Kornel Csach

2016 ◽  
Vol 59 (5) ◽  
pp. 612-617
Author(s):  
A. A. Gavrilyuk ◽  
A. L. Semenov ◽  
A. R. Gafarov ◽  
A. V. Gavrilyuk ◽  
N. P. Kovaleva ◽  
...  

2019 ◽  
Vol 147 ◽  
pp. 592-601 ◽  
Author(s):  
Jianxin Xu ◽  
Qingtai Xiao ◽  
Zhihan Lv ◽  
Junwei Huang ◽  
Ruoxiu Xiao ◽  
...  

2013 ◽  
Vol 2013 ◽  
pp. 1-9 ◽  
Author(s):  
Hameed B. Mahood ◽  
Adel O. Sharif ◽  
Seyed Ali Hosseini ◽  
Rex B. Thorpe

An analytical model for the temperature distribution of a spray column, three-phase direct contact heat exchanger is developed. So far there were only numerical models available for this process; however to understand the dynamic behaviour of these systems, characteristic models are required. In this work, using cell model configuration and irrotational potential flow approximation characteristic models has been developed for the relative velocity and the drag coefficient of the evaporation swarm of drops in an immiscible liquid, using a convective heat transfer coefficient of those drops included the drop interaction effect, which derived by authors already. Moreover, one-dimensional energy equation was formulated involving the direct contact heat transfer coefficient, the holdup ratio, the drop radius, the relative velocity, and the physical phases properties. In addition, time-dependent drops sizes were taken into account as a function of vaporization ratio inside the drops, while a constant holdup ratio along the column was assumed. Furthermore, the model correlated well against experimental data.


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