Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4346749e66e870e1aa782161cdc1168c |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1061 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1038 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1014 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-023 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-006 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0045 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0205 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-031 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-78 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-745 |
filingDate |
2010-02-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_80cccf52566f8d986a10d99d37a69eb0 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c638149e77feabbf2e6ddf2e9e5d529a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_632baaa5d655fe6d00e71945d7a3bd7c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ffc09ff86063da48332df97adc2d319b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dc89ae7b5871e4174ceb5cf0ce2f19e7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2556b49b5da88c5b779982f8ee29725b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_625c8cb8829002722a963d155c6e9a06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0df58ac7bc5634217e419bc081f01a4f |
publicationDate |
2010-06-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-2010152036-A1 |
titleOfInvention |
Precipitated iron catalyst for hydrogenation of carbon monoxide |
abstract |
A method of producing an iron catalyst for catalyzing the hydrogenation of carbon monoxide is disclosed. The method comprises using a reduced amount of acid for iron dissolution compared to certain previous methods. The resulting acidic iron mixture is heated without boiling to obtain a nitrate solution having a Fe 2+ :Fe 3+ ratio in the range of about 0.01%:99.99% to about 100%:0% (wt:wt). Iron phases are precipitated at a lower temperature compared to certain previous methods. The recovered catalyst precursor is dried and sized to form particles having a size distribution between 10 microns and 100 microns. In embodiments, the Fe 2+ :Fe 3+ ratio in the nitric acid solution may be in the range of from about 3%:97% to about 30%:70% (wt:wt) and the calcined catalyst may comprise a maghemite:hematite ratio of about 1%:99% to about 70%:30%. |
priorityDate |
2007-08-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |