http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2662966-T3
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/C07C51-412 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/C12P7-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-035 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-01 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/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> |
| grantDate | 2018-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1dcf8e5810ca5e0758fcc02067ab1fdd http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cf60e5673df46cdce51993f0aad10bfa http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4c857d9f7fe2aceacb35d5a18655d4fa |
| publicationDate | 2018-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2662966-T3 |
| titleOfInvention | Procedure to process magnesium chloride solutions |
| abstract | Process for processing MgCl2 solutions comprising the steps of - providing an aqueous solution comprising 5-25% by weight of MgCl2 and organic pollutants at an evaporation stage, in which water and organic components are evaporated, in the that the product of the evaporation stage has a total content of organic components (TOC) which is a maximum of 50% of the TOC of the aqueous solution provided to the evaporation stage, - removing an aqueous solution with a MgCl2 concentration of a 25-35% by weight of the evaporation step and provide it to a preconcentrator in which it contacts a gas stream containing HCl with a temperature of at least 300 ° C, - providing an aqueous solution with a concentration of MgCl2 35-45% by weight resulting from the preconcentrator to a thermohydrolysis reactor, the reactor being at a temperature of at least 300 ° C, - removing MgO from the thermohydrolysis reactor in f solid form, and removing a gas stream containing HCl from the thermohydrolysis reactor, said gas stream containing HCl having a temperature of at least 300 ° C, - providing the gas stream containing HCl with a temperature of at least 300 ° C to the preconcentrator, - withdraw a gas stream containing HCl with a maximum temperature of 150 ° C from the preconcentrator. |
| 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: 55.