http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-3016909-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_199450d8e2d705a2b559ce4c32e5dcb3 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01P2006-80 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F5-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F5-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-412 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-01 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F5-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B13-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-035 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P7-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P3-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B13-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F5-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F5-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-40 |
| filingDate | 2014-07-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_215db9c0d39ea397f2105a01fe137d5d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cf60e5673df46cdce51993f0aad10bfa http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6af9cc40130de1a02fe3ce70369d7a52 |
| publicationDate | 2016-05-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | EP-3016909-A1 |
| titleOfInvention | Method for processing magnesium chloride solutions |
| abstract | The invention pertains to a method for processing MgC12 solutions comprising the steps of - providing an aqueous solution comprising 5-25 wt. % of MgC12 and optionally organic contaminants to an evaporation step, wherein water and, where present, organic components are evaporated, - withdrawing an aqueous solution with a MgC12 concentration of 25-35 wt. % from an evaporation step and providing it to a preconcentrator where it is contacted with a HC1 containing gas stream with a temperature of at least 300 °C, - providing an aqueous solution with a MgC12 concentration of 35-45 wt. % resulting from the preconcentrator to a thermohydrolysis reactor, the reactor being at a temperature of at least 300°C, - withdrawing MgO from the thermohydrolysis reactor in solid form, and withdrawing a HC1 containing gas stream from the thermohydrolysis reactor, said HC1-containing gas stream having a temperature of at least 300 °C, - providing the HC1-containing gas stream with a temperature of at least 300°C to the preconcentrator, - withdrawing a HC1-containing gas stream with a temperature of at most 150 °C from the preconcentrator. It has been found that the process according to the invention can be integrated into a fermentation process in such a manner that a stable and efficient process is obtained. |
| priorityDate | 2013-07-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 38.