http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2020046152-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_2a30621b245964571b185ac087eb8fdf |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J20-28061 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-001 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C11B3-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23D9-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J20-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J20-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J20-28011 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C11B3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C11B3-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C11B3-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C11B3-14 |
| filingDate | 2019-08-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a6e263e08aab78ad2933786b226ee93e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_56e95d835c63fa193476655e10ae6c09 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6c8b32659a1c4ca49b6a1b77c2347c13 |
| publicationDate | 2020-03-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | WO-2020046152-A1 |
| titleOfInvention | The method of production of refined edible oil with low content of undesirable 3-mpcd, 2-mpcd and glycides |
| abstract | The production process for refined edible oil with low content of undesirable 3-monochloropropane-l,2-diol, 2-monochloropane-l,3-diol and glycides is characterised in that the oil obtained by known methods of pressing, extraction, deguming and neutralisation is subjected to the following steps: preliminary drying of the oil by heating it to the temperature from 90 to 100°C; proper bleaching process with addition of 1 to 2% by weight of bleaching earth with steam activated carbon at the temperature from 90 to 120°C, at the pressure from 60 to 100 mmHg; multi-stage filtration process under conditions of gradual increase of pressure for no longer than 3 hours or until the pressure value of no more than 2 bar is reached; removal of the layer of oily bleaching earth retained on the filter plates after prior purging within 20 to 45 minutes with dry steam at a pressure of 2 to 3 bar; deodorizing process starting from preheating the initial oil to the temperature from 90 to 100°C, and then heating the oil to the temperature from 120 to 125°C using steam at the pressure of 3 bar, drying the oil by spraying it at 20 to 30mmHg pressure and vacuum oil distillation at the temperature from 180 to 18°C, at a pressure not exceeding 5.5mmHg. |
| priorityDate | 2018-08-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 51.