| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_10636948adeff7a4f9c77a5c45be2245 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2240-46
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2240-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2230-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2215-54
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2200-92 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-0409
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04084
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04393
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04381
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04412
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04296
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-0406
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04915
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04054
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04024
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04666
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04678
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04351
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04175
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04109
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-04727 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25J3-04 |
| filingDate |
2018-05-17^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_15f3c693a908eea8b92117fb5dd6e3a0 |
| publicationDate |
2019-08-21^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
TR-201910679-T4 |
| titleOfInvention |
Method and air separation system for the recovery of one or more air products. |
| abstract |
The invention is based on the use of an air separation system 100 with a rectification column system 14-17 comprising a high pressure column 14 and a low pressure column 15 and having a main heat exchanger 9 and a main air compressor. proposes a method for obtaining one or more air products, wherein all air delivered to the rectification column system 10-17 is compressed to a first pressure level inside the main air compressor (1), and the high pressure column (15) is the first pressure and a gaseous, nitrogen-rich fluid is drawn from the high pressure column (15) at the second pressure level and heated to gas without prior liquefaction. A first partial amount of the gaseous nitrogen-rich fluid is heated to a first temperature level of -150 to -100 ° C, in particular -140 to -120 ° C, at that temperature level it is conveyed to a pressure booster 12. and continues to be compressed to a third pressure level using the pressure booster 12, and the first partial quantity is heated to a second temperature level above the first temperature level after compressed to the third pressure level and permanently removed from the air separation system 100. It is stipulated to be shipped. A suitable air separation system 100 is also the subject of the invention. |
| priorityDate |
2017-06-02^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |