Unburned carbon from lignite fly ash as an adsorbent for SO2 removal

The aim of this work is to investigate the possibility of application of unburned carbon from lignite fly ash for the purpose of SO2 adsorption from flue gases. The subject of research are three fraction of unburned carbon, which were formed during the nominal operation of Belchatow Power Station (PGE GiEK) in Poland. In order to characterize the adsorption properties of the investigated materials, a comprehensive research procedure was carried out, including: proximate and ultimate analysis, determination of calorific value, textural characterization (C6H6 and CO2 physisorption, SEM (scanning electron microscope)), surface chemistry characterization (XRD (X-ray diffraction), ICP–OES (inductively coupled plasma-optical emission spectrometry), TPD (temperature-programmed desorption), PZC (point of zero charge)), determination of ignition temperature (DSC (differential scanning calorimetry)) and SO2 adsorption tests using fixed–bed of an adsorbent. Conducted analyses shows, that high carbonaceous wastes, being a result of rapid and intense oxidation of lignite in an industrial boiler, exhibit high potential for adsorption and are characterized by the competitive properties relative to carbon materials, obtained in the laboratory conditions and presented in the literature. It has also been shown, that the chemical nature of adsorbent surface has a significant impact on the effectiveness of SO2 adsorption and on the adsorbate selectivity. Own research demonstrates, that an increase of sulphur dioxide adsorption is observed with an increase of the oxygen surface groups content, i.e. carboxylic acids and lactones, which formation is favoured in conditions prevailing in the industrial boiler. Own research, dedicated to determination of ignition temperature of unburned carbons, confirmed the validity of application of DSC analysis for this purpose. The research results, presented in this work show, that unburned carbons from lignite fly ash, in particularly UN–B and UN–C, have competitive surface structure properties relative to commercially available activated carbons: AKP–5 and AKP–5/A, and can be successfully used as adsorbents for flue gases desulphurization.

[1]  M. Izquierdo,et al.  Influence of activation atmosphere used in the chemical activation of almond shell on the characteristics and adsorption performance of activated carbons , 2014 .

[2]  G. Furdin,et al.  SO2 adsorptive properties of activated carbons prepared from polyacrylonitrile and its blends with coal-tar pitch , 2009 .

[3]  M. Izquierdo,et al.  Low cost coal-based carbons for combined SO2 and NO removal from exhaust gas , 2003 .

[4]  D. Cazorla-Amorós,et al.  Factors controling the SO2 removal by porous carbons: relevance of the SO2 oxidation step , 2000 .

[5]  Gerrit Brem,et al.  Modelling spontaneous ignition of wood, char and RDF in a lab-scale packed bed , 2013 .

[6]  Karl Knoblauch,et al.  Application of active coke in processes of SO2- and NOx-removal from flue gases☆ , 1981 .

[7]  P. Davini Adsorption and desorption of SO2 on active carbon: The effect of surface basic groups , 1990 .

[8]  D. Cazorla-Amorós,et al.  The role of different nitrogen functional groups on the removal of SO2 from flue gases by N-doped activated carbon powders and fibres , 2003 .

[9]  F. Xing,et al.  The Pore Structure of Phosphoaluminate Cement , 2012 .

[10]  K. Jastrząb Properties of activated cokes used for flue gas treatment in industrial waste incineration plants , 2012 .

[11]  M. Izquierdo,et al.  Influence of low-rank coal char properties on their SO2 removal capacity from flue gases: I. Non-activated chars , 1997 .

[12]  M. Izquierdo,et al.  Unburnt carbon from coal fly ashes as a precursor of activated carbon for nitric oxide removal. , 2007, Journal of hazardous materials.

[13]  A. Dalai,et al.  Preparation and characterization of chars and activated carbons from Saskatchewan lignite , 2006 .

[14]  Robert H. Hurt,et al.  A Kinetic Model of Carbon Burnout in Pulverized Coal Combustion , 1998 .

[15]  J. Figueiredo,et al.  Modification of the surface chemistry of activated carbons , 1999 .

[16]  M. N. Mohamed,et al.  Evaluation of thermal hazards and thermo-kinetic parameters of a matchhead composition by DSC and ARC , 2013 .

[17]  M. Izquierdo,et al.  Coal fly ash based carbons for SO2 removal from flue gases. , 2010, Waste management.

[18]  M. Izquierdo,et al.  Carbon-enriched coal fly ash as a precursor of activated carbons for SO2 removal. , 2008, Journal of hazardous materials.

[19]  M. Izquierdo,et al.  Enhancement of nitric oxide removal by ammonia on a low-rank coal based carbon by sulphuric acid tre , 2011 .

[20]  N. N. Semenov,et al.  Some problems in chemical kinetics and reactivity , 1958 .

[21]  N. Mitan,et al.  Characterization of biochar derived from rubber wood sawdust through slow pyrolysis on surface porosities and functional groups , 2013 .

[22]  E. Teller,et al.  On a Theory of the van der Waals Adsorption of Gases , 1940 .

[23]  E. Fuente,et al.  Adsorbents/catalysts from forest biomass fly ash. Influence of alkaline activating agent , 2015 .

[24]  F. Fernández-Martínez,et al.  Adsorption of SO2 onto waste cork powder-derived activated carbons , 2012 .

[25]  K. J. Hüttinger,et al.  Surface-oxidized carbon fibers: I. Surface structure and chemistry , 1996 .

[26]  F. Carrasco-Marín,et al.  Regularities in the temperature-programmed desorption spectra of CO2 and CO from activated carbons , 2000 .