http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101920827-B1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a9d3c71872d0db755c851805f8ed7a99 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-804 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-708 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02A50-20 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-8687 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-86 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D46-0036 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23G7-07 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-74 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-75 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0407 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61L9-205 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-005 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D46-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-75 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61L9-20 |
| filingDate | 2018-02-21^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2018-11-26^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_99a330035b5adca9e7cb6e9457d62202 |
| publicationDate | 2018-11-26^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-101920827-B1 |
| titleOfInvention | Indoor Concentrated and Combustion System of VOCs with Catalytic Poison Oxidation device |
| abstract | An indoor concentrated combustion system having a catalytic poison oxidizer of the present invention collects volatile gas at room temperature and includes a VOCs gas collecting unit installed on the front surface of a zeolite concentrator of a rectangular box shape, A prefilter for removing particulate matter from a substance contained in the VOCs gas captured by the gas trapping unit and a VOCs gas passing through the prefilter is filtered by a method of adsorbing volatile substances in the zeolite thickening unit, And the air is supplied to the 449 ° C output line of the ceramic catalytic oxidation unit by connecting the 139 ° C output line thereof to the output line of the ceramic catalytic oxidation unit. The high temperature air of 449 ° C of the ceramic catalytic oxidation unit is cooled to a predetermined temperature (200 ° C) The volatiles in the zone are desorbed and removed and sent to the heat exchanger using a desorption blower. A main blower connected to the zeolite concentrator at the rear of the zeolite concentrator and configured to exhaust gas into which the volatile materials have been removed from the zeolite concentrator; Temperature air of 449 ° C from the ceramic catalytic oxidation unit to be used for heat exchange and the 196 ° C gas used in the heat exchanger is supplied to the ultraviolet lamp section And the exhaust gas is discharged to the outside through a process gas outlet. The heat exchanger is installed inside the body, and the gas having 220 ° C containing volatile substances is transferred from the heat exchanger By receiving and heating the heated gas to a ceramic catalytic oxidation facility, An electric heater installed in an upper part of the heat exchanger in the body part; and a heating unit for receiving the volatile material heated by the electric heater, oxidizing the volatile substance using the catalyst, supplying hot air of 449 ° C to the heat exchanger, And a low temperature air of 139 占 폚 transferred from an output line of the concentrator is mixed and supplied to a zeolite concentrator to desorb and remove volatile substances in the adsorption zone. The catalytic oxidation facility is disposed on the other side of the heat exchanger inside the body, And a heat exchanger disposed at a lower portion of the catalytic oxidizer and disposed at the lower portion of the catalytic oxidizer, wherein the gas is used for heat exchange and desorbed and removed from the volatile material to remove the bus gas and residual gas causing the catalyst poison, And an ultraviolet lamp part formed on one side of the ultraviolet lamp part, It is characterized in that is configured to receive the gas transferred from the lamp unit to the process gas discharge port for discharging to the outside. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114191936-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-116571058-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114522500-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114534464-A |
| priorityDate | 2018-02-21^^<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 36 of 36.