http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-4283371-A
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_bdc01940a960a8185530dba5afbbb488 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F7-62 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F7-62 |
filingDate | 1980-01-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 1981-08-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cd30aee1f53f9ae6cd17e1a4b8e57673 |
publicationDate | 1981-08-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | US-4283371-A |
titleOfInvention | Process for the production of aluminum chloride and related products |
abstract | A continuous process for recovering substantially pure aluminum chloride from chlorination products of aluminum ore. The chlorination products are contacted with a first selective solvent to dissolve a substantial portion of the aluminum chloride and some ferric chloride. The solvent is separated from the chlorides which then are treated to produce a ferric chloride-rich stream and an aluminum chloride-rich stream in which the aluminum chloride to ferric chloride ratio is higher than the ratio prior to solvent separation. The aluminum chloride-rich stream is contacted with a second solvent to dissolve any ferric chloride present and saturate the solution with aluminum chloride. Aluminum chloride in excess of that soluble in the second solvent separates as a substantially pure solid phase. The solution is separated from solid phase and recycled in process to recover additional aluminum chloride. |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-4853205-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-4457812-A |
priorityDate | 1980-01-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 53.