http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101205442-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-10 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C09K5-042 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C09K5-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25B1-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25B49-00 |
| filingDate | 2008-11-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2012-11-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2012-11-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-101205442-B1 |
| titleOfInvention | Hydrocarbon mixed refrigerant, refrigeration or air-conditioning air conditioning system, refrigeration or air-conditioning air conditioning method, and method of manufacturing refrigeration or air-conditioning air conditioning system |
| abstract | By replacing the Freon's replacement Freon (HCFC, HFC) with a hydrocarbon refrigerant of natural refrigerant to enable non-freonization by the hydrocarbon refrigerant of the natural refrigerant to reduce the replacement Freon to save energy in the refrigeration air conditioner. The hydrocarbon-mixed refrigerant of the present invention contains propane, the saturated vapor pressure at 7 ° C is 0.3 to 1 MPa, and the saturated vapor pressure at 35 ° C is 0.6 to 2.2 MPa. You may further contain n-butane, isobutane, and ethane. The boiling point of the hydrocarbon mixed refrigerant is preferably -20 ° C or lower. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101754225-B1 |
| priorityDate | 2007-12-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 54.