http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-111138292-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_67f4b0724a1f689319e16dfc78146be8 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J27-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0093 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C211-15 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-21 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-25 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-087 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C209-08 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C211-15 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C17-087 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C19-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C209-08 |
| filingDate | 2019-10-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9522f7b7a6bcee6586cfeb868b6fc230 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_05be7026a7898c3f98e9638e3bce546a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5ca7c695daa65741308b05de68a21176 |
| publicationDate | 2020-05-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-111138292-A |
| titleOfInvention | Process for the manufacture of 1,1,1-trifluoro-2-chloroethane and/or trifluoroethylamine |
| abstract | The present invention relates to a process for the production of 1,1,1-trifluoro-2-chloroethane (HCFC-133a) and/or trifluoroethylamine (TFEA), wherein at least one reaction step is in a microreactor conduct. In particular, preferred embodiments of the present invention relate to a process for the production of 1,1,1-trifluoro-2-chloroethane (HCFC-133a) and/or trifluoroethylamine (TFEA), wherein at least one of The reaction steps are carried out in microreactors constructed or fabricated from SiC ("SiC microreactors") or in microreactors constructed or fabricated from alloys such as Hastelloy C. In the manufacture of HCFC-133a and/or TFEA, HCFC-133a and/or TEFA can be readily purified and/or isolated, for example, using only low-energy-consuming methods, and the method of purification and/or isolation preferably does not require Distilled. Advantageously, HCFC-133a and/or TEFA can be easily and energy-efficiently separated from excess HF and catalyst by phase separation. |
| priorityDate | 2018-11-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 62.