http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2625009-T3
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_664f5b543543aac4cf0153a4ef4e0f85 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2256-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-4145 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40047 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-4068 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-108 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/B01D2259-40041 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40026 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40045 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40075 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-047 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-047 |
| filingDate | 2012-01-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2017-07-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a8a56fbbf0581279ac1322152bb4539b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e85a19803e08be785514a9b85f5e1359 |
| publicationDate | 2017-07-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2625009-T3 |
| titleOfInvention | Large-scale pressure variation adsorption systems with process cycles that operate in normal and reduction mode |
| abstract | A pressure swing adsorption process for separating a pressurized supply feed gas containing one or more more strongly adsorbable components from at least one less strongly adsorbable product gas component in an eleven-bed pressure swing adsorption system to produce a continuous stream of product gas enriched in the less strongly adsorbable component and a continuous stream of outlet gas that is enriched in strongly adsorbable components, wherein the process cycle has four stages of bed-by-bed equalization, while four of the beds are in production, and use purge gas of increasing concentrations of less strongly adsorbable product gas during the purge stages, based on the following cycle table:**Table** where: A1 >= First Stage stage A2 >= Second stage adsorption A3 >= Third stage adsorption A4 >= Fourth stage adsorption A5 >= Fifth stage adsorption cap A6 >= Sixth adsorption stage A7 >= Seventh adsorption stage A8 >= Eighth adsorption stage E1 >= First equalization down E2 >= Second equalization down E3 >= Third equalization down E4 >= Fourth equalization down PPG1 > = First supply of purge gas PPG2 >= Second supply of purge gas BD >= Emptying PG2 >= Purge using gas from stage PPG2 PG1 >= Purge using gas from stage PPG1 E4' >= Upward equalization (using gas from stage E4) E3' >= Upstream equalization (using gas from stage E3) E2' >= Upstream equalization (using gas from stage E2) E1' >= Upstream equalization (using gas from stage E1) PP >= Pressurization of the product |
| priorityDate | 2011-01-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
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