| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_09106e43404d6b1977281e2561a126e1 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-80
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-702
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-116
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-108
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-106
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-104
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-102
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L2290-60
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2256-245
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L2290-542
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-4145 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0462
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L3-101
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L3-106
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0407
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0423 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10L3-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-02 |
| filingDate |
2019-07-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_50bb09176572d6ccb380572733fa5333
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_73d94a3001b4b7a1c2b1bf1a4cbcd596
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_aa4b693760158a1cc84491ac7cf0448d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bc40c33d811586b6007cea16946f6b20 |
| publicationDate |
2021-02-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
AU-2019308257-A1 |
| titleOfInvention |
Processes for removing heavy hydrocarbons and water from a stream of natural gas |
| abstract |
Process for retrofitting existing processing units for natural gas fee streams. A portion of the dehydration adsorbent is removed from the vessels of the dehydration unit and is replaced with an adsorbent for heavy hydrocarbons. In operation the vessels are operated in thermal swing adsorption processes with reduced cycle times compared to the original design. |
| priorityDate |
2018-07-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |