| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9d9aa0fe053f8d1f33cfb48f2e4a7c2d |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-102
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-91
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-4533
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-25
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40009
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-4009
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2258-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61M2202-0241
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-2066
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2253-108 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C41-36
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-389
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0438
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0462
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0415
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61M16-0093
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61M16-1065
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61M16-1045 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C41-36
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C17-389 |
| filingDate |
2020-02-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_75a517d956c702efb8a2154404852476
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a1cf357efe640043a48fd2a6d607f4fc |
| publicationDate |
2022-04-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2022111326-A1 |
| titleOfInvention |
Two-stage method for recovering halogenated hydrocarbons |
| abstract |
The invention relates to a two-stage method for recovering halogenated hydrocarbons. In a desorption step, steam is passed through an adsorbent comprising adsorbed halogenated hydrocarbons, which produces a secondary flow volume containing halogenated hydrocarbons. The secondary flow volume is converted into a condensate containing halogenated hydrocarbons and water by cooling, from which condensate the halogenated hydrocarbons are separated. In a sterilisation step that precedes the desorption step, the adsorbent comprising adsorbed halogenated hydrocarbons is brought into contact with steam for at least 10 minutes at a temperature of more than 120° C. and at a pressure between 0.15 MPa and 0.4 MPa. |
| priorityDate |
2019-02-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |