| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9080d63f8da0a644b6e7b9fcdcf6f306 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S423-05 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-504
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-502
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-508
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-501
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-34 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-34
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-50
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F11-06 |
| filingDate |
1995-05-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9c45efd5ab508cce05067ccdbbda7eaa
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_aa5e26adb74f738c5eec8c3c669a5022
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_17c5e3c7a68f620e9d22a08117675802
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dff2dadd15bd61856689b20bb8285cac
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_622147fbeca64730354b2bb64b215fe4
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2a7340ff36681664ed1cd80efcc075d4
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fdf34f82a588413cf2a7fd4865afed24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3a50f97995389e923e80c06eeccebd75 |
| publicationDate |
2004-05-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CZ-293501-B6 |
| titleOfInvention |
A method for desulphurisation of wet-type flue gases and apparatus for its implementation |
| abstract |
A wet type flue gas desulfurization method and apparatus using a solid desulfurizing agent in which the flue gases are contacted with a water-containing absorbing liquid as a major component to absorb sulfur oxides from the flue gases into an absorbing liquid, followed by neutralization of the absorbing liquid containing the sulfur oxides thus absorbed. The solid desulfurizing agent is selectively retained in the neutralization zone to neutralize the absorbing liquid, having a weighted average particle diameter of Ź mm or greater and selectively withdrawing the water-containing absorbing liquid as the main component and the solids formed from the sulfur oxides from the neutralization zone based on having a weighted mean particle diameter of less than ŹŹ mm, wherein the absorption liquid from the neutralization zone is partially recirculated back into contact with the flue gas. Tz formed absorption tower}} Bz inlet passage and an outlet passage @B @}} Bz spray nozzles and manifold @B @ B @} also includes the neutralization apparatus, and recirculating aparátŕ |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107694311-A |
| priorityDate |
1994-05-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |