| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d6a6f422b091ba12ea61d4adbf1b0e8e |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10J3-72
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10J3-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10J3-84 |
| filingDate |
2015-03-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
2015-07-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e1dbc9d2b0aa0f6344582d16bcaece4f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9e54a2a3c7f5bf29f9c7cd23db5c7a53
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3009ee4f7dfe23d62e9116aa87c8017e
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c8ca5f7ef006dd77d0fd4e57f1073e01
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6cb89d8b6185542e433fb39ddd1ef0b5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6e5d9843bf812d39dc1a03c51f4f4f87
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_618ae4974975ba6540a1128c93a4e454
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_97681c227c20758bc9b0ef91e620dabd
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_68415c4932b1bab57bb3e38a06d23679
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_43bcb81da69a945137867598a70c5a86
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e2e1b5662f5e39dd87c7a76ca0462139 |
| publicationDate |
2015-07-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CN-204509222-U |
| titleOfInvention |
A kind of U-shaped fixed bed gasification-catalyst reaction device with tar degradation function |
| abstract |
There is disclosed in the utility model the U-shaped fixed bed gasification-catalyst reaction device of tar degradation function, mainly comprise downdraft fixed bed gasification reactor, updraft type catalytic cracking reaction device and cyclonic separator.Downdraft fixed bed gasification reactor has feeding device and blowing system; the trend of flue gas in stove is U-shaped; and whole U-shaped reactor is all in high-heat region and protected by thermal insulation layer; to ensure that the tar ingredients after gasifying can not condensed along journey tube-cooled, thus enter catalytic cracking reaction device in the form of a vapor and fully decompose in catalyticreactor.After the utility model solves current waste gasification, gas product is coal-tar middle oil and particle content is too high and the problems such as the gas product purification cost increase that causes. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-112019002562-B4
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105505470-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105505470-B
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105349184-B
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105349184-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104774650-A |
| priorityDate |
2015-03-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |