http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-1904429-A4
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_33c922e05f6133b7d72dbb849d77487d |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-025 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-0004 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00212 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-0053 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-36 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-252 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-215 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0457 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0453 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-34 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-37 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-35 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-067 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-27 |
filingDate | 2006-07-07-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ebddab963676012f56b0e5684148b665 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_44dbcbbae88c2b6796a47c38a9814663 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_45f25c4b77b503a4cab8947b306ef386 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_075681e2d99dd27861dfbc2ee7009002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_57e842af6c93a0d820f21132a260930e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e97dae8c3a0d88420dbe21809e59de26 |
publicationDate | 2009-02-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | EP-1904429-A4 |
titleOfInvention | METHOD FOR PRODUCING UNSATURATED ACIDITY IN A HIGH EFFICIENCY CATALYTIC FIXED BED OXIDATION REACTOR |
abstract | Disclosed is a process for producing unsaturated aldehydes and/or unsaturated acids from olefins or alkanes in a fixed bed shell-and-tube heat exchanger-type reactor by catalytic vapor phase oxidation. A heat exchanger-type reactor for use in such a process is also disclosed. In the process, at least one of the first-step reaction zone and the second-step reaction zone is divided into two or more shell spaces by at least one partition; each of the divided shell spaces is independently heat-controlled; a heat transfer medium in the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone has a temperature ranging from the lowest active temperature of a catalyst layer packed in a reaction tube corresponding to the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone to [the lowest active temperature + 20 °C], when referring to the two or more shell spaces corresponding to the first-step reaction zone sequentially as the first shell space of the first-step reaction zone, the second shell space of the first-step reaction zone, ..., the nth shell space of the first-step reaction zone, and the two or more shell spaces corresponding to the second-step reaction zone sequentially as the first shell space of the second-step reaction zone, the second shell space of the second-step reaction zone, ... , the nth shell space of the second-step reaction zone; and the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone is controlled in such a manner that the first shell space provides a reactant conversion contribution per length as defined in Equation 1 or 2 of 1.2∼2.5. |
priorityDate | 2005-07-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 37.