Predicate |
Object |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-42 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2303-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2103-365 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-722 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2209-003 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2101-101 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-469 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-725 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F9-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-008 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F11-086 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-46 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D61-48 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D61-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-74 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-469 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-42 |
filingDate |
2007-12-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate |
2010-09-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
JP-2010530793-A |
titleOfInvention |
System and method for process flow processing |
abstract |
Systems and methods for process flow processing. The treatment system can generally include an oxidation unit coupled downstream of the desalination unit. The oxidation unit can oxidize organic reduced sulfur contaminants in the process stream to facilitate downstream processing. The desalination unit can convert the product of the oxidation unit to produce a mineral stream. In some examples, the process stream may be a spent caustic stream from an industrial plant such as an ethylene production facility or an oil refinery. It is possible to isolate a fresh caustic stream, such as a sodium hydroxide stream, in a desalting step and return it to an industrial operation. [Selection] Figure 1 |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2012011377-A |
priorityDate |
2006-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |