http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114053958-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_caacf483b6be9ae2d2677103a70559db http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ab49e79a04d810d2beb56541efd130f3 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0285 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-008 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-00 |
| filingDate | 2021-12-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e420e5081e5e96acdc482e385b477d98 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f85607b68c102729b107e737b76ea84f |
| publicationDate | 2022-02-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-114053958-A |
| titleOfInvention | A braided tube heat exchange fixed bed reactor and its application |
| abstract | A braided tubular heat exchange fixed bed reactor and application thereof belong to the technical field of reaction engineering. In this braided tube type fixed bed reactor, the heat exchange unit is made of M groups, N groups, and P groups of heat exchange tubes woven into heat exchange mats, and then the heat exchange mats are rolled around the mandrel or the radial bed distributor. There are more than two scroll reels of different diameters. One end of the M group, N group and P group heat exchange tubes of the scroll drum is connected to the tube side inlet on the first head, and the other end is connected to the tube side outlet on the second head. The structure of the heat exchange tube braided by the vortex drum increases the heat transfer area and improves the heat transfer performance. At the same time, the multi-stream heat exchange structure of the reactor is realized, and the heat can be dissipated in time during the reaction. , to prevent the occurrence of overheating. In addition, the heat exchange process is further optimized by arranging different types of distributors inside the reactor. For the reactor with radial bed distributor, under the same cylinder diameter, it has a larger flow cross-sectional area. |
| priorityDate | 2021-12-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 35.