Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4486ba4389f74a5daff26d886b869c55 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c4f814e21d521de0bfc1dff1d5b5edc4 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-44 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D11-0492 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G53-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D11-0488 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G21-27 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G21-28 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G7-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G21-00 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C7-10 |
filingDate |
2013-02-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
2014-03-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_349d14397aeed333f324d3684673e045 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a5e2b7f57e4b1a1a0ce5d2e808b719fb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5c907a6e6a37255c2b723623d023bffa http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b9f25db87390a43ed4504a99806658ad http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b63596f3c4a49208b89e6a7f4e95d000 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_79ee49c5171ad4c7f3bdcc712b8c2144 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_64a422b298b52070c9cbc38d77f3fe58 |
publicationDate |
2014-03-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-8680358-B1 |
titleOfInvention |
Methods for removing heavy hydrocarbons from extractive solvents |
abstract |
A method for cross connecting the lean solvent supply lines between the liquid liquid extraction (LLE) and the extractive distillation (ED) processes thereby using the LLE column as the outlet for removing accumulated heavy hydrocarbons (HCs) and polymeric materials from the solvent loop of both processes to maintain their solvent performance. The unique capabilities of the LLE column in rejecting heavy HCs from the solvent into a raffinate product stream that leaves the system enable the removal of the accumulated heavy HCs and polymeric materials from the closed solvent loop of the ED process when their lean solvent loop are cross connected. Cross connection requires minimum equipment change. In the revamped system, the solvent recovery column (SRC) in LLE process supplies lean solvent for the extractive distillation column while the SRC of the ED process supplies lean solvent for LLE column. |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10392322-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-110032552-B http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-110032552-A |
priorityDate |
2013-02-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |