http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114017785-A
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a6ffa780fba85318d018e4f06db5d61a |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23G5-442 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F26B25-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F26B25-005 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23M7-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23G7-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F26B23-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23G5-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23G5-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F26B21-14 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G5-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G7-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F26B21-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F26B23-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23M7-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F26B25-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F26B25-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G5-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G5-44 |
filingDate | 2021-11-05^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_93ffc0ad146e5be3ad8e95ff92d6d459 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1fa86759ff3a9b49c05cc731d584f8d6 |
publicationDate | 2022-02-08^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-114017785-A |
titleOfInvention | Reclaimed material asphalt flue gas incinerator flue gas heat energy recycling device and process |
abstract | The invention relates to a reclaimed material asphalt flue gas incinerator flue gas heat energy recycling device and a process, which comprise a reclaimed material drying system A, a reclaimed material drying system B and a reclaimed material flue gas incinerator C, wherein the gas outlet end of the reclaimed material drying system B is respectively communicated with the gas inlet end of the reclaimed material flue gas incinerator C and the gas inlet end of the reclaimed material drying system A, the gas outlet end of the reclaimed material flue gas incinerator C is communicated with the gas inlet end of the reclaimed material drying system A, and the gas outlet end of the reclaimed material drying system A is communicated with the atmosphere through a dust removal device. The high-temperature flue gas generated by the asphalt flue gas treatment equipment incinerator is fully utilized, the high-temperature flue gas with the temperature of 1000 ℃ which exceeds the process temperature of 760 ℃ specified by asphalt flue gas incineration is directly used as drying and heating of new aggregates, the treatment efficiency of the asphalt flue gas is improved under the treatment of higher incineration temperature, and the high-temperature flue gas is used as heat energy supply for drying and heating of the new aggregates, so that the heat transfer efficiency is further improved at higher exhaust gas temperature, and the high-efficiency energy-saving environment-friendly asphalt flue gas treatment equipment is high-efficiency and energy-saving. |
priorityDate | 2021-11-05^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Showing number of triples: 1 to 32 of 32.