http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105358484-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01P2006-80 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-01 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B13-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P7-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-035 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F5-10 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 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-40 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/C01B13-18 |
| filingDate | 2014-07-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2018-02-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2018-02-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-105358484-B |
| titleOfInvention | The method for handling magnesium chloride solution |
| abstract | The present invention relates to processing MgCl 2 The method of solution, comprises the following steps：5 25wt%MgCl will be included 2 Evaporation step is supplied to the aqueous solution of optional organic pollution, water therein and organic component that may be present is evaporated, MgCl is taken out from evaporation step 2 Concentration be 25 35wt% the aqueous solution, provide it to preconcentrator, wherein the aqueous solution at a temperature of at least 300 DEG C with the air flow contacts containing HCl, the MgCl that will be obtained by preconcentrator 2 Concentration is that the 35 45wt% aqueous solution is supplied to pyrohydrolysis reactor, the temperature of the reactor is at least 300 DEG C, the MgO of solid form is taken out from pyrohydrolysis reactor, with air-flow of the taking-up containing HCl from pyrohydrolysis reactor, the air-flow containing HCl has at least 300 DEG C of temperature, the air-flow containing HCl of at least 300 DEG C temperature is supplied to preconcentrator, the air-flow containing HCl of at most 150 DEG C temperature is taken out from preconcentrator.Fermentation process can be integrated into this way to obtain stable and efficient method by having found the inventive method. |
| 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: 53.