http://rdf.ncbi.nlm.nih.gov/pubchem/patent/TW-201002649-A
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_8e0bf0928b608797b70bbc2b91c7e52e |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2601-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00777 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C29-147 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J4-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-246 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C29-19 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-025 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-228 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-2465 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C209-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-226 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B35-02 |
filingDate | 2009-05-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1237633eafe5208cd0f8b3315b9d4215 |
publicationDate | 2010-01-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | TW-201002649-A |
titleOfInvention | Continuous process and reactor for hydrogenating organic compounds |
abstract | The present invention relates to a continuous process for hydrogenating organic compounds in a polyphasic system in the presence of a homogeneous or heterogeneous catalyst, which comprises performing the process in two stages, the first stage being performed in a loop reactor with an external heat exchanger and the second stage in a bubble column reactor with limited backmixing. The present invention further relates to a hydrogenation reactor (1) in a tall cylindrical design comprising a concentric guide tube (2) arranged in the lower reaction region and a mixing nozzle (3) directed upward, through which reactants and reaction mixture can be supplied, a pump (4) and a heat exchanger (5), which are present in an external pump circulation system which leads from the reactor to the mixing pump, and with one or more gas- and liquid-permeable internals (10) mounted in the upper region of the reactor, where the ratio of total length to diameter of the hydrogenation reactor (1) is in the range from 5: 1 to 100: 1 and the ratio of the volume of the upper region of the reactor to the volume of the lower region of the reactor is from 0.05: 1 to 10: 1. |
priorityDate | 2008-05-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 75.