http://rdf.ncbi.nlm.nih.gov/pubchem/patent/GB-888672-A
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_2b6f417d8aa0ab6740f79d8d0ec55a96 |
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classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-464 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C5-2791 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-40 |
classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J21-08 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-27 |
filingDate | 1959-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f51226088822a5bbeca27a8e1323e44a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fd2d2f87c248d412dbcbea3c1e6c1f63 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_835e8cebd56408b98deef21ccff20105 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_07555f191ca4c76bac8d4356f25b1f20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6f4f278de5fd891861d4d99372e2847d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3825e7a373b3e511c3ebce9ea1df07ec http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_aac5e3938b1718c7657ead426746ba2b |
publicationDate | 1962-01-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | GB-888672-A |
titleOfInvention | Improvements in or relating to isomerising hydrocarbons |
abstract | A hydrocarbon isomerization catalyst comprises 0,1-1% palladium or rhodium on a support containing 50-95% silica and the balance alumina, and optionally 10-60% (based on the noble metal) of an iron group metal, particularly nickel or cobalt. The catalyst support is calcined at 524 DEG -593 DEG C. for 1-4 hours and, after impregnation, is activated by reducing with hydrogen at 413 DEG -555 DEG C., purging, oxidizing with free oxygen at 413 DEG -555 DEG C., purging, and again reducing at 400 DEG -524 DEG C. and 28-40 atmospheres. Regeneration may be effected by oxidizing with an oxygen partial pressure above a minimum line given in Fig. 2 (not shown) at 343 DEG -510 DEG C. with less than 15 mm. Hg partial pressure of water followed by reduction at 400 DEG -510 DEG C. Specifications 720,388, 823,010 and 825,353 are referred to.ALSO:A feed comprising n-pentane and/or n-hexane is isomerised by contact with a catalyst containing 0.1%-1% palladium or rhodium supported on an acidic cracking support containing 50%-95% silica and 50%-5% alumina to effect at least 30% conversion at a selectivity of at least 97% at 343 DEG C-421 DEG C., 8-80 atmospheres and with hydrogen to give a hydrogen to hydrocarbon mol ratio of 0.5-5. The catalyst may be promoted by the addition of an iron group metal, particularly nickel or cobalt in an amount of 10%-60% based on the noble metal. The feed should contain less than 3 p.p.m. sulphur and 15% (volume) of cyclopentane or heavier hydrocarbons. The space velocity may be 0.5-10 vol./vol./hr. The catalyst support is preferably calcined at 524 DEG C.-593 DEG C. for 1-4 hours and after impregnation is activated by reducing at 413 DEG C.-555 DEG C. with hydrogen, purging, oxidising with free oxygen at 413 DEG C.-555 DEG C., purging and again reducing at 400 DEG C.-524 DEG C. and 28-40 atmospheres. The catalyst may be regenerated by oxidising with an oxygen partial pressure above the minimum line given in Fig. 2 (not shown) and 343 DEG C.-510 DEG C. with less than 15 mm. Hg. water partial pressure and reducing at 400 DEG C.-510 DEG C. Specifications 720,388, 823,010 and 825,353 are referred to. |
priorityDate | 1959-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 54.