http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2467372-A1

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c75f1afc3f5c07fce3df1db39c987ea0
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-00
filingDate 2004-05-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1ea8c529533d20482591948e88c1a8ce
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_842825ca33461e391279f4b5c6bd2802
publicationDate 2005-11-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CA-2467372-A1
titleOfInvention Process and apparatus for converting oil shale or oil sand (tar sand) to oil
abstract Three new embodiments to the Chattanooga Process that convert or upgrade oil bitumen, a combination of oil sands and bitumen, a combination of sand and bitumen, and oil shale to high grade low sulfur (about 0.1 to 0.5 wt.% sulfur, or less) crude oil. The invention relates to a continuous process for producing synthetic crude oil (SCO) from oil sand bitumen which has been extracted from under ground via in situ processes, or strip mined and extracted via hot water extraction processes before upgrading. It can also apply to kerogen extracted in situ from shale underground. The process involves treating the hot bitumen with sand from an extraction process or the hot kerogen with ground shale containing kerogen in a fluid bed reactor where the reactant and fluidizing medium is only hydrogen. The invention also relates to a continuous process for producing synthetic crude oil (SCO) from oil shale kerogen. The invention relates to a continuous process for producing synthetic crude oil from ail bearing material, e.g., oil shale or oil sand (tar sand), through continuous process for producing synthetic crude oil from bituminous oil sand (tar sand) or shale. The process includes treating the oil sand (tar sand) or shale to produce a fluidizable feed, feeding the fluidizable feed to a fluidized bed reactor, and fluidizing and reacting the fluidizable feed in the fluidized bed reactor with a feed of hydrogen provided by a feed stream having a stream containing hydrogen in a concentration greater than 90 vol % (90 vol % - 100 vol % H2).
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8968579-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2012085408-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8968580-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8025341-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7736501-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/FR-2969651-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8800784-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8168071-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8096425-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9016799-B2
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http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7726491-B2
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priorityDate 2004-05-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 38.