http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2379075-T3
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_577821cf81fda3e1088e6ed08bcd136b |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B2009-168 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61K9-1694 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61K9-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61K9-1623 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F26B17-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B9-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B7-94 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B7-483 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29C48-92 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29C48-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29C48-022 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23P10-25 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29C48-834 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29C48-402 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B29B9-08 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J2-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B29B7-48 |
filingDate | 2003-11-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2012-04-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_323967d3cd253ec130408cd64b47b270 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0d3a5ec6b6a4962cf5835aa979cdc854 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2210081504574f51b7e7b9e4d5379615 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d8d4bb662bd9ad9d67ce35abe2876d0c |
publicationDate | 2012-04-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | ES-2379075-T3 |
titleOfInvention | Process and apparatus for continuous wet granulation of powder material |
abstract | An apparatus for continuous wet granulation of a powder material, consisting essentially of: - a barrel having a granulation chamber provided between a first upper part (B) and a second upper part (B ') of said barrel, being said first upper part (B) provided with at least a first inlet (1) connected with said granulation chamber to receive said powder material and to deliver it to said granulation chamber and with at least a second inlet (2) connected with said granulation chamber for receiving a granulation liquid and for supplying it to said granulation chamber, said granulation chamber having an opening (9) for discharging granules from said barrel, - at least one continuously operated transport means (S) provided in said granulation chamber to advance said powder material towards the end of said granulation chamber, while said powder material is granulated with the aid of said granulation liquid, each of said transport means (S) comprising at least a first transport zone (4) at its rear end and optionally one or more additional transport zones (6), an agglomeration zone (5) downstream of the first transport zone (4) and optionally one or more additional agglomeration zones (7), and a second transport zone (8) at its front end, each agglomeration zone (5, 7) between two transport zones (4, 6, 8) and contributing to advance the powder material, said at least one first entrance (1) and said at least one second entrance (2) of the barrel being positioned above the at least one first transport zone (4) of each of at least one transport means (S), said at least one second entrance (2) being separated from said at least one first entrance (1) and said position being positioned at least a second entry (2) between said at least one prime The inlet (1) and the agglomeration zone (5) downstream of the first transport zone (4), wherein said opening (9) has a shape that fits slightly with the terminal portion of said at least one means transport (S) to directly discharge said granules from the granulation chamber without developing a pressure gradient at the outlet of the granulation chamber. The second transport zone (8) is a granule formation zone. |
priorityDate | 2002-11-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 552.