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description Publicationkeyboard_double_arrow_right Conference object 2018 ItalyS. Krusch; V. Scherer; R. Solimene; G. Ruoppolo; O. Senneca;In the present work different methodologies have been used to analyze pyrolysis of a German bituminous coal "Auguste Victoria" with the aim to obtain pyrolysis kinetic submodels suitable for combustion models developed under Barracuda or other CFD environment such as Ansys Fluent. Intrinsic kinetics have been obtained by conventional TGA analysis at low heating rate (2-20 K/min) and with small particle size (in the order of 0.1 mm) and described by a two-step pyrolysis model. Additionally, the rates of pyrolysis were measured under fluidized bed conditions for larger particle size fractions using a method based on the time-resolved measurement of pressure in the freeboard induced by volatiles release and by a flow restriction at the exhaust. Results of thermogravimetric experiments have been worked out to obtain submodels of coal pyrolysis, comparing and discussing alternative reaction networks of different complexity. However, in fluidized bed experiments, using larger particle sizes, transport limitations become important. As expected, for this regime the reactions rates become lower the larger the particle size, reducing the relevance of intrinsic kinetic submodels.
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For further information contact us at helpdesk@openaire.eudescription Publicationkeyboard_double_arrow_right Conference object 2016 ItalyB. Apicella1; O. Senneca1; C. Russo1; F. Stanzione1; L. Cortese; A. Ciajolo1; V. Scherer2; S. Heuer;The early stages of coal oxy-combustion and pyrolysis were investigated in a drop tube furnace operated at 1300°C with different O2/N2/O2/CO2 atmosphere. The different types of carbonaceous solids produced at short residence times (50-100 ms) in the tube were separated to discriminate soot from incipient char for further analysis. In particular, a procedure involving dispersion in ethanol by ultrasonic mixing, followed by settling, and decanting to produce top and bottom products enriched in the coarse and fine particle fractions, respectively, was set up for separating soot from char. The procedure was repeated several times and the separation efficiency was checked by electron microscopy and size determination. Soot and char, separated and weighted after solvent removal, can be further characterized by a wide array of techniques in order to highlight the differences between them and their relation with the atmosphere employed. Beside electron microscopy and laser granulometry, thermogravimetry, elemental analysis and spectroscopic analysis (UV-visible and FT-IR absorption, RAMAN) were applied to soot and char for giving insights on the determination of the conditions under which the amount of soot and its chemical and physical characteristics are of practical significance for full-scale power plant particulate emissions and ash disposal.
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more_vert add ClaimPlease grant OpenAIRE to access and update your ORCID works.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.All Research productsarrow_drop_down <script type="text/javascript"> <!-- document.write('<div id="oa_widget"></div>'); document.write('<script type="text/javascript" src="https://beta.openaire.eu/index.php?option=com_openaire&view=widget&format=raw&projectId=cnr_________::6001fa27f09333848bdefb60df1010ee&type=result"></script>'); --> </script>
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description Publicationkeyboard_double_arrow_right Conference object 2018 ItalyS. Krusch; V. Scherer; R. Solimene; G. Ruoppolo; O. Senneca;In the present work different methodologies have been used to analyze pyrolysis of a German bituminous coal "Auguste Victoria" with the aim to obtain pyrolysis kinetic submodels suitable for combustion models developed under Barracuda or other CFD environment such as Ansys Fluent. Intrinsic kinetics have been obtained by conventional TGA analysis at low heating rate (2-20 K/min) and with small particle size (in the order of 0.1 mm) and described by a two-step pyrolysis model. Additionally, the rates of pyrolysis were measured under fluidized bed conditions for larger particle size fractions using a method based on the time-resolved measurement of pressure in the freeboard induced by volatiles release and by a flow restriction at the exhaust. Results of thermogravimetric experiments have been worked out to obtain submodels of coal pyrolysis, comparing and discussing alternative reaction networks of different complexity. However, in fluidized bed experiments, using larger particle sizes, transport limitations become important. As expected, for this regime the reactions rates become lower the larger the particle size, reducing the relevance of intrinsic kinetic submodels.
add ClaimPlease grant OpenAIRE to access and update your ORCID works.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.All Research productsarrow_drop_down <script type="text/javascript"> <!-- document.write('<div id="oa_widget"></div>'); document.write('<script type="text/javascript" src="https://beta.openaire.eu/index.php?option=com_openaire&view=widget&format=raw&projectId=cnr_________::52ef2bcce2fe1088d3c37e9dea6e08a7&type=result"></script>'); --> </script>
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more_vert add ClaimPlease grant OpenAIRE to access and update your ORCID works.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.All Research productsarrow_drop_down <script type="text/javascript"> <!-- document.write('<div id="oa_widget"></div>'); document.write('<script type="text/javascript" src="https://beta.openaire.eu/index.php?option=com_openaire&view=widget&format=raw&projectId=cnr_________::52ef2bcce2fe1088d3c37e9dea6e08a7&type=result"></script>'); --> </script>
For further information contact us at helpdesk@openaire.eudescription Publicationkeyboard_double_arrow_right Conference object 2016 ItalyB. Apicella1; O. Senneca1; C. Russo1; F. Stanzione1; L. Cortese; A. Ciajolo1; V. Scherer2; S. Heuer;The early stages of coal oxy-combustion and pyrolysis were investigated in a drop tube furnace operated at 1300°C with different O2/N2/O2/CO2 atmosphere. The different types of carbonaceous solids produced at short residence times (50-100 ms) in the tube were separated to discriminate soot from incipient char for further analysis. In particular, a procedure involving dispersion in ethanol by ultrasonic mixing, followed by settling, and decanting to produce top and bottom products enriched in the coarse and fine particle fractions, respectively, was set up for separating soot from char. The procedure was repeated several times and the separation efficiency was checked by electron microscopy and size determination. Soot and char, separated and weighted after solvent removal, can be further characterized by a wide array of techniques in order to highlight the differences between them and their relation with the atmosphere employed. Beside electron microscopy and laser granulometry, thermogravimetry, elemental analysis and spectroscopic analysis (UV-visible and FT-IR absorption, RAMAN) were applied to soot and char for giving insights on the determination of the conditions under which the amount of soot and its chemical and physical characteristics are of practical significance for full-scale power plant particulate emissions and ash disposal.
add ClaimPlease grant OpenAIRE to access and update your ORCID works.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.All Research productsarrow_drop_down <script type="text/javascript"> <!-- document.write('<div id="oa_widget"></div>'); document.write('<script type="text/javascript" src="https://beta.openaire.eu/index.php?option=com_openaire&view=widget&format=raw&projectId=cnr_________::6001fa27f09333848bdefb60df1010ee&type=result"></script>'); --> </script>
For further information contact us at helpdesk@openaire.eu0 citations 0 popularity Average influence Average impulse Average Powered by BIP!
more_vert add ClaimPlease grant OpenAIRE to access and update your ORCID works.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.This Research product is the result of merged Research products in OpenAIRE.
You have already added works in your ORCID record related to the merged Research product.All Research productsarrow_drop_down <script type="text/javascript"> <!-- document.write('<div id="oa_widget"></div>'); document.write('<script type="text/javascript" src="https://beta.openaire.eu/index.php?option=com_openaire&view=widget&format=raw&projectId=cnr_________::6001fa27f09333848bdefb60df1010ee&type=result"></script>'); --> </script>
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