Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7549d655c106f6c1ba7de93e8356509d |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02W30-62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2020-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2050-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1003 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2020-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2070-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2030-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J2323-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2030-24 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10M2205-163 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10M2205-143 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2030-68 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10N2020-019 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10M107-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J11-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10M101-025 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08J11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C4-08 |
filingDate |
2011-07-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
2015-04-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d01607bbf6825e34132f0c06a319a522 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b168189c51ffb7de30a6f3029e727360 |
publicationDate |
2015-04-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
CN-103168016-B |
titleOfInvention |
Method and producing waxes and grease base stocks through catalytic depolymerisation of waste plastics |
abstract |
A process of depolymerization of mixed polyethylene waste is disclosed. In one embodiment, in a process for converting mixed polyethylene waste to make waxes and grease base stocks through catalytic depolymerization, the mixed polyethylene waste is preheated to form a molten mixed polyethylene waste. Then depolymerization reaction of the molten mixed polyethylene waste is started. The depolymerization reaction uses a catalyst in a high pressure reactor at a desired temperature using heaters in the high pressure reactor. The catalyst is disposed on a stirring blade. Progression of depolymerization reaction of the molten mixed polyethylene waste is allowed to continue until a pressure in the high pressure reactor reaches a desired value.; The heaters are turned off and depolymerization reaction of the molten mixed polyethylene waste is stopped upon the pressure in the reactor reaching desired value. The mixed polyethylene waste is converted to wax or grease base stock. |
priorityDate |
2010-07-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |