http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-H0970520-A

Outgoing Links

Predicate Object
assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_74973199515dbabd2310245aab03e282
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-94
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86
filingDate 1995-09-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c9473b91efcb1b32c47deb5e5bb3c686
publicationDate 1997-03-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber JP-H0970520-A
titleOfInvention Ammonia recovery device
abstract (57) [PROBLEMS] To provide a leak ammonia recovery device configured such that the gas flow during desorption is uniform and uniform, and ammonia can be recovered with high efficiency. SOLUTION: An adsorbent tank 8 is provided downstream of an exhaust gas denitration device. Arrange A and 8B almost vertically. At the time of adsorption, the low-temperature exhaust gas containing ammonia moves upward from below the adsorbent tanks 8A and 8B, and at the time of desorption, the high temperature gas for desorption is the same. The duct, piping, and damper system are configured to flow downward from above A and 8B. High temperature gas bypass duct 10 serving as a supply pipe for high temperature gas for desorption and adsorbent tanks 8A, 8B A swirl duct 21 equipped with swirl fins 22 is provided between and to provide a swirl flow to the desorption high-temperature gas flowing into the adsorbent tanks 8A and 8B. As a result, the gas flow in the adsorbent layer during desorption becomes uniform.
priorityDate 1995-09-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

Incoming Links

Predicate Subject
isDiscussedBy http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID419550829
http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID222

Total number of triples: 14.