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filingDate 2014-10-02^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0d504607fa842c71e3ea9195cddb8b92
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publicationDate 2016-08-25^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber US-2016245508-A1
titleOfInvention Waste sludge incinerator using pyrolysis and gasification, and relative process
abstract The present invention relates to reaction equipment for the treatment of organic and/or inorganic waste of refineries or petrochemical plants comprising: •—a drying and pyrolysis device ( 4 ) which rotates around its longitudinal, tilted rotation axis (A), •—a gasification device ( 6 ) which rotates around its longitudinal, horizontal rotation axis (B), •—a combustion device ( 14 ) comprising a burner ( 13 ) having a longitudinal horizontal axis (C), •—at least one settling chamber ( 15 ) for the collection of intermediate solid residues and the accumulation of intermediate gaseous reaction products, •—at least one outlet duct of the gaseous end-products ( 16 ), at least one outlet duct of the solid end-products ( 7 ), and at least one inlet duct of the feedstock ( 2 ) •—said combustion device ( 14 ), drying and pyrolysis device ( 4 ), gasification device ( 6 ) are physically separated and positioned on three different levels, •—the longitudinal rotation axis (A) of the drying and pyrolysis device ( 4 ) is tilted with respect to both the longitudinal rotation axis (B) of the gasification device ( 6 ) and also with respect to the longitudinal axis (C) of the combustion device ( 14 ), •—the longitudinal rotation axis (B) of the gasification device ( 6 ) is parallel to the longitudinal axis (C) of the combustion device ( 14 ), •—the combustion device ( 14 ) is in fluid communication with the drying and pyrolysis device ( 4 ), •—the drying and pyrolysis device ( 4 ) comprises, in its interior, a first indirect heat exchange device ( 3 ) in which the combustion fumes coming from the combustion device ( 14 ) flow, •—at least one settling chamber ( 15 ) in fluid communication with said drying and pyrolysis device ( 4 ) and with said gasification device ( 6 ) and with said combustion device ( 14 ), •—conveying means ( 5 ) are positioned in the settling chamber ( 15 ) and put the drying and pyrolysis device ( 4 ) in fluid communication with the gasification device, •—it comprises a second heat exchange device ( 12 ) in fluid communication with the first indirect heat exchange device ( 3 ) and the combustion device ( 14 ), •—it comprises means for the suction of the intermediate gaseous reaction products, said means being positioned in the settling chamber ( 15 ).
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http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9841190-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2021041099-A1
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http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11555610-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2015338092-A1
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priorityDate 2013-10-03^^<http://www.w3.org/2001/XMLSchema#date>
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