http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-206355802-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_53b4d53983adbf56dd0e7d0bf96f8ce5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c0a77cb144a9c41ed237b1f2c1ead3a1 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-78 |
| filingDate | 2016-11-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2017-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7d73a4f50eca6872f0454456d2de89da http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_07b4c129b6fd404cd6e36f7a231a239b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_755f5169b93ff737a55f6c16f1f43fcb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5bdac5a3d20cffa497e5282dcde497de http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c140c452e733cbe284f6d48e93b6ae22 |
| publicationDate | 2017-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-206355802-U |
| titleOfInvention | A kind of hydrogen peroxide method flue gas desulfurization processing system |
| abstract | The utility model provides a kind of hydrogen peroxide method flue gas desulfurization processing system.The desulfurization process system includes the reactive absorption tower of four layers of design of single column, hydrogen peroxide holding vessel, circulating pump, circulating slot and chimney；Wherein the floor of reactive absorption tower four is that demisting floor is absorption tower first layer, circulation fluid room i.e. the absorption tower second layer, absorbed layer i.e. absorption tower third layer and the gas mixer chamber i.e. floor of absorption tower the 4th.Desulfurization process system architecture of the present utility model is simple, convenient operation and control, and its desulfuration efficiency is high；And processing system corollary equipment is few, without additionally increasing operating personnel, effectively save cost of investment, operating cost and floor space, more than 98% desulfuration efficiency can be realized, in the absence of the stifled tower problem of crystallization, its byproduct dilute sulfuric acid is not required to secondary operation, and cost recovery is low, three new waste products, and non-secondary pollution are not produced in whole production process. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107899403-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107890763-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114634832-B http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114634832-A |
| priorityDate | 2016-11-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 35.