http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2010043509-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_fec2d42202a3728e8aea158ffd353646 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d7d3eab93b08c4171b630c2af85bfa7e |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02A40-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02W30-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2103-322 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-145 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F11-086 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C05F5-002 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C05F11-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C11B13-02 |
| filingDate | 2007-12-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2111485bb2f353b3638cbfef0e2b8d8a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dacd06ccc6cb2fe02bbd176970759def http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bcc753f4a99b477fbc5f27962ff8bbea http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_63f3bc8dac5d5e898a6f4a033bf8731e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ea35e0cb36f3b83f57ffb9843a193cef |
| publicationDate | 2010-02-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | US-2010043509-A1 |
| titleOfInvention | Soapstock treatment apparatus, soapstock treatment method, and method for manufacturing fertilizer derived from soapstock |
| abstract | Disclosed is a soapstock treatment apparatus which can treat a soapstock produced during a plant oil production process within a short period and with a high degree of efficiency. As shown in FIG. 1, the soapstock treatment apparatus includes a reactor 20 configured to oxidatively decompose a soapstock, an electric heating coil 23 configured to heat water in the reactor 20 at 650° C. which is not less than the critical temperature of water, a high-pressure pump 13 configured to pressurize the water in the reactor 20 at 17 Mpa which is less than the critical pressure of water, and a compressor 33 configured to pressurize the water in the reactor 20 at 17 Mpa which is less than the critical pressure of water. Also, an exhaust pipe 41 for discharging a reaction gas generated by the oxidative decomposition treatment and a waste pipe 51 for discharging a solid (inorganic) residue generated by the oxidative decomposition treatment are connected to the reactor 20. Furthermore, a gas-liquid separator 44 for separating the reaction gas into a gas substance and a liquid substance are connected. |
| priorityDate | 2007-02-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 35.