http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-206635100-U
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ac31afbea1cbbb03498644721ffb4a62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_cbcc06148f54da6f60ce5713f80fa94c |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F9-04 |
filingDate | 2017-03-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2017-11-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2c693d62d653e8ea1d06bc5d3a2dc3c7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8785f6fc4b11034a8b7d4618d997c5a4 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_134404fe16110eb73ee6692f34bd004b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8a5a4dfa8feca2d2ffc672786f1a05d0 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c30cb74b944a9a7c5cee6510c5590279 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_32fceb77abb876dea77dbb591662e7c9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9c88b8cea634f904a877bc05dafcd801 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9d9c05eb3a1d55482228357390671530 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_889d0b5b469970885c4a0d4523d234d9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2370cf180c7311eece7844337b8d6147 |
publicationDate | 2017-11-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-206635100-U |
titleOfInvention | A kind of integral type gradient ozone catalytic fluidized bed plant |
abstract | The utility model discloses a kind of integral type gradient ozone catalytic fluidized bed plant, the device includes the first-stage reactor set gradually from bottom to top, second reactor, third-stage reactor and level four reaction apparatus, wherein, the bottom of first-stage reactor is provided with water inlet and ozonation aerated device, its top is provided with circulation water inlet, the first catalyst layer and the second catalyst layer are respectively equipped with described second reactor and third-stage reactor, the top of third-stage reactor is provided with delivery port and circulating outlet, circulation water inlet is connected by reflux pump and circulation pipe with circulating outlet, and circulation water inlet is set with reactor body in upward corner cut.Integral type gradient ozone catalytic fluidized bed plant of the present utility model improves the utilization rate and the catalysis oxidation efficiency of ozone, make catalytic oxidation more efficient, complete, compact reaction mechanism is used simultaneously, course of reaction is completed in same device, floor space is smaller. |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-106630110-A |
priorityDate | 2017-03-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 32.