| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0efa077d881a96aeb1e29b21ef1bbb58 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00212 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-38
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-67
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0242
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-087 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-67
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C47-22
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C47-21
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-38
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-52 |
| filingDate |
1998-05-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3ad33e5560870c29991efefc8853a80b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1a72fbb9698c6743635e5ba19e4c8479
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_29438e3b5720f19f3fadd7c0a47142c5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4ce3076370acd14bd85e43bdefce6403
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0df1c4578d6c980b0def65533ecf954d |
| publicationDate |
1998-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
JP-H10338656-A |
| titleOfInvention |
Process for continuous industrial production of aldehydes |
| abstract |
PROBLEM TO BE SOLVED: To improve an industrial production method of an unsaturated aliphatic aldehyde so that it can be operated for several years without equipment interruption and costly perforation of a reaction tube. SOLUTION: General formula II [R 1 is hydrogen, R 2 is Or R 1 and R 2 together Is evaporated, an oxygen-containing gas is added, and the obtained oxygen-containing alcohol vapor is heated at a temperature higher than the dew point of the alcohol but lower than the starting temperature of the reaction. The vapor is passed through one layer of the supported catalyst, after which the oxygen-containing alcohol vapor is passed through about 0. The reaction with the corresponding aldehyde is carried out at a temperature of from 300 to 600 ° C. in a reaction tube having an internal diameter D of 5 to 3 cm and a length of 5 cm or more. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2012531392-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2011513283-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2014516770-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2011515361-A |
| priorityDate |
1997-05-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |