http://rdf.ncbi.nlm.nih.gov/pubchem/patent/TW-200911127-A
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_442006254efb98c9cebec6ee5a08d5e8 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D11-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A23D9-00 |
filingDate | 2007-09-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5665a2e09359556b9cbd69d94e25fd0c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_25d1cef4783e4dc2b63b7f7c3f6f78e2 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b9865c1dbeb687ba2456e6fef7580a3d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_270eb412a20d858aa9e42a72d9d37298 |
publicationDate | 2009-03-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | TW-200911127-A |
titleOfInvention | Process of using supercritical CO2 in extraction/distillation tower with θ-type fill-net to remove free fatty acid in rice bran oil |
abstract | The invention discloses a process of using supercritical CO2 in extraction/distillation tower with θ-type fill-net to remove free fatty acid in rice bran oil. The extraction/distillation process is that the 2700g CO2 at the temperature of 353K and the pressure of 200bar is filled into the 27 cm high extraction tank with θ-type net to deacidify the rice bran oil having the free fatty acids with the concentration of 10% so as to obtain a deacidification oil having 0.26% free fatty acid. This invention is characterized by having the best effect of deacidification. |
priorityDate | 2007-09-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 18.