| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_1e70c0aeade92d7571d955d3b90ea06e
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_86127fdceca51d646f705221d1a4e17b |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-205
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-202
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1077
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1055
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-107
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1037
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-802 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G49-26
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-22
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-72
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-36
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-00 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-00 |
| filingDate |
2006-03-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_13fec8bc393ebc6d69f707a9942a5a3a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_86749611d9e0dcd7f02148424d1c8fd4 |
| publicationDate |
2016-02-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
BR-PI0612172-B1 |
| titleOfInvention |
method and apparatus for continuous liquid phase hydroprocessing control system |
| abstract |
Method and apparatus for continuous liquid phase hydroprocessing control system, characterized in that the need to circulate hydrogen gas or to have a separate hydrogen phase through the catalyst has been eliminated. This is achieved by mixing and / or sparking the hydrogen and oil to be treated in the presence of a solvent or diluent having a relatively high solubility for hydrogen in a constant pressure environment so that hydrogen is part of the solution. Excess hydrogen is mixed and / or centered in the oil / diluent solution so that the maximum capacity of the oil / hydrogen diluent solution is utilized. hydrogen in excess of the amount soluble in the oil / diluent solution remains in the vapor phase. |
| priorityDate |
2005-03-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |