http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8183423-B2
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f3287b33ee9db6958b38e7b97d799bc8 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29K2707-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02W30-62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29K2021-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29L2030-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29K2105-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J2321-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4006 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B2017-0496 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29K2105-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1003 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J11-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B17-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-10 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B31-00 |
| filingDate | 2006-12-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2012-05-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_771a5e86b4861e0ab39c9a3de17c138b |
| publicationDate | 2012-05-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | US-8183423-B2 |
| titleOfInvention | Pyrolysis process for waste and old rubber |
| abstract | This invention is about a cracking technology of waste rubber, and the content of this technology is as following: the rubber mass with the catalyst were added in the cracking chamber and the cracking process of the raw material is finished. The main contents and weight percentage of catalyzer are as following: the aluminosilicate is from 35 to 50, the active alumina is from 15 to 30, the zinc oxide is from 10 to 20, the active argil is from 5 to 15, the kaoline is from 5 to 15, the weight ratio of catalyst and rubber is 2-7:1000; The cracking temperature is from 350 to 450° C. The rubber mass crack comparative downright in low temperature by using this combinatorial catalyst, that's because the temperature is controlled between 350 and 450° C., which commendably control the cracking process of the carbon chain of rubber. Moreover, more low carbon chain products can be gained for the symmetrical cracking. Therefore, the emerging ratio of the oil will become higher, the exhaust gas emission will become lower and the eligible emission will really come ture. |
| priorityDate | 2006-12-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 36.