http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2331179-T3
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_8e0bf0928b608797b70bbc2b91c7e52e |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C5-333 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J27-199 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-33 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-35 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C47-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C253-26 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-333 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-35 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-34 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C51-235 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C255-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C57-055 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J27-199 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-33 |
| filingDate | 2002-06-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2009-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_23e4212adc5f3d1a9b211bdef4429c4c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c1f36d6d6670926e5324deb028df3556 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fd5b8603d23fbf09248593f7692ab909 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_672f8ce7c332ab10fdb68ad0672b59d5 |
| publicationDate | 2009-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2331179-T3 |
| titleOfInvention | PROCEDURE FOR OBTAINING PRODUCTS OF PARTIAL OXIDATION AND / OR PRODUCTS OF PARTIAL AMOXIDATION OF, AT LEAST, AN OLEFINIC HYDROCARBON. |
| abstract | Procedure for obtaining partial oxidation products and / or partial amoxidation products of at least one olefin hydrocarbon A '' '', in which A) in a first reaction zone A, at least one paraffinic hydrocarbon A is subjected to a dehydrogenation and / or a partial oxyhydrogenation, forming a mixture of products A, which contains an unconverted amount of at least one paraffinic hydrocarbon A and at least one olefinic hydrocarbon A '' 'obtained by dehydrogenation and / or partial oxyhydrogenation, B) separates, from the mixture of products A, a part or all of the components found in said mixture of products A, said components being different from at least the only paraffinic hydrocarbon A and the at least, only olefinic olefinic hydrocarbon A '' '', possibly, in a separation zone, and the mixture of products A or the mixture of products A '' '' is used to feed an oxidation zone and / or amoxidation B and in the zone of oxidation and / or amoxidation B, at least, the, at least unique, olefinic hydrocarbon A '' '' is subjected to oxidation and / or partial amoxidation, forming a mixture of products B, containing, as a desired product, at least one oxidation and / or partial amoxidation product B of the at least unique olefinic hydrocarbon A '' '', C) the desired product is separated from the mixture of products B in an area of processing C and, at least a part of the at least single, unconverted paraffinic hydrocarbon A, contained in the mixture of products B, is redirected as paraffinic hydrocarbon return A to the reaction zone A and D) from time to time At least a partial amount of the reaction zone A is not used, during a non-operative phase, for the purpose of dehydrogenation and / or partial oxyhydrogenation of the at least single paraffinic hydrocarbon A, characterized in that during the non-operative phase of at least the amount pa The reaction zone A continues to drive the oxidation and / or amoxidation zone B and, in addition, the loss of production of the at least single olefinic hydrocarbon, associated with the non-operational phase, is compensated, at least partially , because at least one olefinic hydrocarbon A '' '' is supplied to the oxidation and / or amoxidation zone B from a different source of reaction zone A and, eventually, one or multiple paraffinic hydrocarbons A from another source other than the reaction zone A, and at least a partial amount of the paraffinic hydrocarbon A which is then in the mixture of products B of the oxidation and / or amoxidation zone B, does not return, as a return paraffinic hydrocarbon A, through the reaction zone A, to the oxidation and / or amoxidation zone B. |
| priorityDate | 2001-06-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 75.