http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101356910-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-52 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J2300-1276 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J2300-0946 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02W30-82 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J3-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J3-16 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10J3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G5-027 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B09B3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10B53-00 |
| filingDate | 2012-02-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2014-01-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2014-01-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-101356910-B1 |
| titleOfInvention | Syngas generating device of organic car waste and its method |
| abstract | The present invention relates to a syngas generating apparatus and method of organic automobile waste, and more specifically, to the waste organic matter discharged from the waste vehicle, water and oil (compared to less than 18%) in the composite gas and carbides generated at low temperature pyrolysis. Carbide and composite gas containing water and oil are sent to the synthesis gasification reactor to reduce it to synthesis gas without using a steam supply device, and to use it as fuel, and carbide, which is a secondary waste generated during pyrolysis, is also used. By gasification. The present invention relates to a syngas generating device for organic automobile waste and a method thereof for drastically reducing secondary waste and pollutants. To this end, the syngas generating apparatus through low temperature pyrolysis according to the present invention is characterized in that waste organic matter (especially waste tires, ASR, etc.) generated from automobiles is contained in the waste properties so as to contain water and oil of 18% (by weight). With a low temperature pyrolysis furnace to pyrolyze at 270 ℃ ~ 450 ℃; A cooling furnace cooling the carbide discharged from the low temperature pyrolysis furnace to a low temperature (less than 50 ° C.); A separator for separating the discharge discharged from the cooling furnace into metal, nonferrous metal, and carbide; A grinder for grinding the carbide selected from the sorter into a powder form; A first vacuum pump for receiving powder in the form of carbide from the mill and supplying the upper portion to a synthesis gasification reactor and a second vacuum pump for introducing a complex gas introduced from the low temperature pyrolysis into a lower portion of the synthesis gasification reactor; A synthesis gas reactor for receiving synthesis gas and powdered carbide from the first and second vacuum pumps; A heat exchanger for heat-exchanging hot gas discharged from an outlet of the synthesis gasification reactor; A refrigerator for secondarily cooling the gas first cooled by the heat exchanger; A separator for removing nitrates and sulfur oxides contained in the gas cooled second by the refrigerator; It consists of a syngas storage tank for storing the gas flowing from the separator. On the other hand, the method of producing a synthesis gas is equipped with a low-temperature pyrolysis furnace for decomposing waste organic matter containing 18% of moisture and oil by the low-temperature pyrolysis method in the range of 270 ℃ ~ 450 ℃ according to the shape of the waste organic matter. A low temperature pyrolysis step of producing carbide and complex gas; A transfer step of transferring the carbides decomposed into fine particles generated in the low temperature pyrolysis step together with the composite gas to the secondary vacuum pump 220; A sorting step of separating the solids discharged from the cooling furnace into metals and carbides; Supplying powdered carbide to the upper portion of the synthesis gasification reactor, and supplying the composite gas and the fine particle carbide introduced by the secondary vacuum pump to the lower portion of the synthesis gasification reactor; A reduction reaction delay step of extending the reaction time of the carbide in powder form introduced into the synthesis gasification reactor in order to increase the reaction efficiency; A first reduction reaction step of performing a reduction reaction while maintaining the lower portion of the synthesis gasification reactor at about 1260 to 1300 ° C .; A second reduction reaction step of passing the first reduction reaction carbide to a top of a synthesis gasification reactor at 1250 ° C .; The third reduction reaction step of passing a high temperature gas through the interior of the discharge portion mounted on the synthesis gasification reactor maintained at 1200 ℃. Synthetic gas generating apparatus and method of the organic car waste of the present invention made as described above, compared to the conventional gasification (reformer) device which is dualized by the conventional reduction reactor and oxidation reactor, it consists of a single refractory brick and the conventional refractory brick and gas Compared with the burner method, the refractory tube and the electric heater method are adopted, and the configuration is simple, and the homogenization of the gasification reaction temperature can be maintained. Therefore, the initial manufacturing cost is low and the maintenance cost can be drastically reduced. In addition, by mounting a plurality of inclined plate having a separate downward inclination angle in the synthesis reactor of the present invention, it is possible to maximize the reduction efficiency according to the synthesis gas production by increasing the reaction time of the carbide. And, due to the reduction method consisting of multiple (1st to 3rd order), Compared with the combustion apparatus, which is an oxidation reaction, the reduction reaction can increase the efficiency of reforming, maximize the production of syngas, and greatly improve the energy efficiency using waste heat discharged to the outlet. The present invention adopts a multi-stage reduction method consisting of a temperature deviation method (bottom: 1300 ℃, top: 1250 ℃, discharge portion: 1200 ℃), it is possible to increase the reforming efficiency and significantly reduce energy consumption compared to the conventional reforming method. It works. In addition, the present invention, by using electricity as a heating source, compared to the method of heating the inside of the reactor using a conventional burner, the long life of the device and easy to use, low maintenance costs, safe and safe during operation It can also be expected to dramatically reduce the effects. |
| priorityDate | 2012-02-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
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