http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-212476586-U
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ed9441b6f7bf41e338e40b8eb2497bfb |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C49-403 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-00 |
filingDate | 2020-04-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2021-02-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d048aa8e802af5bf314eb32b4f6890df http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f3194b8b0d40d3e6e4662cd61dda7658 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_18c5006499bca28c68cd3fc08fbd5e16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e3c64636891a886343b66b5e06986b81 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_97c6fa0d3cf5d5796ddf1a3da831572c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4b3796a8e1638f6750160c33e7018ea5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_13f2bfce75f6014817c2de6ca5315c52 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0d261f62ab30958f2189f075ddfeca2e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4d5126ddd43d81532b7c64f8b0b299b3 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ab6305d62ca4d84ecf9efb98d5ea5bbe http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6ccdacafb3bde91152d2d01b3184a7c2 |
publicationDate | 2021-02-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-212476586-U |
titleOfInvention | Heat energy comprehensive utilization system suitable for cyclohexanone device |
abstract | The utility model relates to a heat energy comprehensive utilization system suitable for a cyclohexanone device, which comprises an alcohol dehydrogenation reaction system and an alcohol dehydrogenation feed preheater; the alcohol dehydrogenation reaction system comprises an alcohol dehydrogenation reactor, an alcohol dehydrogenation evaporator, an alcohol dehydrogenation heat exchanger, a cyclohexanol liquid separation tank and a flow control regulating valve; the material outlet of the alcohol dehydrogenation feed preheater is connected with the material inlet of the alcohol dehydrogenation evaporator, and the flow control regulating valve is arranged between the alcohol dehydrogenation evaporator and the alcohol dehydrogenation feed preheater; the gas phase outlet of the cyclohexanol liquid separating tank is communicated with a material inlet pipeline of the alcohol dehydrogenation reactor through an alcohol dehydrogenation heat exchanger; exchanging heat between the material flowing out of the alcohol dehydrogenation reactor and the material before entering the alcohol dehydrogenation reactor; the heat brought out from the alcohol dehydrogenation reactor and the cooled cold material are comprehensively utilized, the heat energy consumption and the circulating water consumption of the alcohol dehydrogenation reactor are reduced, and the comprehensive utilization of the heat energy is facilitated. |
priorityDate | 2020-04-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 33.