The application of membrane separator arranged in series-parallel mode to removal of carbon dioxide from flue gases generated in heat and power industry

2017 ◽  
Vol 64 ◽  
pp. 359-364
Author(s):  
Grzegorz Wiciak
1991 ◽  
Vol 24 (7) ◽  
pp. 277-284 ◽  
Author(s):  
E. Gomólka ◽  
B. Gomólka

Whenever possible, neutralization of alkaline wastewater should involve low-cost acid. It is conventional to make use of carbonic acid produced via the reaction of carbon dioxide (contained in flue gases) with water according to the following equation: Carbon dioxide content in the flue gas stream varies from 10% to 15%. The flue gas stream may either be passed to the wastewater contained in the recarbonizers, or. enter the scrubbers (which are continually sprayed with wastewater) from the bottom in oountercurrent. The reactors, in which recarbonation occurs, have the ability to expand the contact surface between gaseous and liquid phase. This can be achieved by gas phase dispersion in the liquid phase (bubbling), by liquid phase dispersion in the gas phase (spraying), or by bubbling and spraying, and mixing. These concurrent operations are carried out during motion of the disk aerator (which is a patent claim). The authors describe the functioning of the disk aerator, the composition of the wastewater produced during wet gasification of carbide, the chemistry of recarbonation and decarbonation, and the concept of applying the disk aerator so as to make the wastewater fit for reuse (after suitable neutralization) as feeding water in acetylene generators.


2012 ◽  
Vol 16 (5) ◽  
pp. 3043-3053 ◽  
Author(s):  
J.C.M. Pires ◽  
M.C.M. Alvim-Ferraz ◽  
F.G. Martins ◽  
M. Simões

1998 ◽  
Vol 37 (1) ◽  
pp. 185-191 ◽  
Author(s):  
Hiromu Hayashi ◽  
Jun Taniuchi ◽  
Nobuyoshi Furuyashiki ◽  
Shigeru Sugiyama ◽  
Shinichi Hirano ◽  
...  

1973 ◽  
Vol 56 (1) ◽  
pp. 119-123
Author(s):  
Martin J Finkelson

Abstract A gas-solid chromatographic method is described for the separation and determination of 5 medicinal gases at ambient temperature, using 2 gas chromatographic columns, Porapak Q and Molecular Sieve 13X, operated in series with a 6-port thermal conductivity detector and I recorder. An electronic digital integrator is used for calculating peak areas. Data on retention time, linearity, reproducibility of injection, and comparison with absorption methods are presented. Analytical results for oxygen, nitrogen, carbon dioxide, ethylene, and nitrous oxide are attainable within 1.0% without the use of an internal standard.


RSC Advances ◽  
2015 ◽  
Vol 5 (89) ◽  
pp. 72469-72475 ◽  
Author(s):  
Debashis Sahu ◽  
Bishwajit Ganguly

The efficient capture and storage of flue gases is of current interest due to environmental problems. The DFT calculation demonstrates the origin of the physisorption of flue gases (CO2, N2and CH4) on amorphous solid cucurbit[7]uril.


Sign in / Sign up

Export Citation Format

Share Document