| 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/C12P7-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-01
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B13-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-412
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P3-00
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/C01B7-035
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F5-10 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P3-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B7-03
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F5-10 |
| filingDate |
2014-07-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6af9cc40130de1a02fe3ce70369d7a52
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_215db9c0d39ea397f2105a01fe137d5d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cf60e5673df46cdce51993f0aad10bfa |
| publicationDate |
2016-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2016369302-A1 |
| titleOfInvention |
Method for processing magnesium chloride solutions |
| abstract |
A method for processing MgCl2 solutions including the steps of: providing an aqueous solution including 5-25 wt. % of MgCl2 and optionally organic contaminants to a step, wherein water and present, organic components are evaporated; withdrawing aqueous solution with a MgCl2 concentration of 25-35 wt. % from an evaporation step and providing it to a preconcentrator where it is contacted with a HCl containing gas stream at least 300° C.; providing aqueous solution with a MgCl2 concentration of 35-45 wt. % resulting from the preconcentrator to a thermohydrolysis reactor, being at at least 300° C.; withdrawing MgO from the thermohydrolysis reactor in solid form, and withdrawing a HCl containing gas stream from the thermohydrolysis reactor, said HCl-containing gas stream at least 300° C.; providing the HCl-containing gas stream with at least 300° C. to the preconcentrator; withdrawing a HCl-containing gas stream with a temperature of at most 150° C. from the preconcentrator. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11261467-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11326188-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11326189-B2 |
| priorityDate |
2013-07-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |