http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-5017281-A

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filingDate 1989-05-30^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1991-05-21^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c48cf300ec94d016bc2e1f4c0d84c66f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8b7a5e43e0e323cd29035bf34881c97d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8ba6ac9d43843215ea75fc3690cccfc6
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publicationDate 1991-05-21^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber US-5017281-A
titleOfInvention Treatment of carbonaceous materials
abstract Hydrocarbon liquids are recovered from carbonaceous materials such as tar sands utilizing a separation reagent formed in situ by reacting polar resin components of tar sands with an inorganic base such as sodium silicate in sonicated aqueous solution in absence of an organic solvent to form a surfactant. Under the influence of sonication a microemulsion of polar-external micelles forms. The polar groups can associate with anions, especially polyanions such as silicate and act in a membrane mimetic manner to form vesicles. Cavities can form in the surfactant resin molecule that complex with guest cations such as titanium or other metals from the tar sand. When tar sands are added to the sonicated separation reagent, the surfactant penetrates the bitumen. Metal ions complex with the polar groups and aid in removing the bitument from the sand particles. The polarorganic asphaltene materials are carried into the aqueous phase by the anion and stabilized within the micelle structure. The lighter, non-polar hydrocarbon oil fraction separate from the emulsion and rise to the top and are recovered by skimming. The heavier asphaltenes and preasphaltenes complex with the polyvalent metals to form charcoal-like agglomerates which settle to the bottom of the treatment tank. The separation reagent forms during the reaction and can reach a concentration capable of dissolving bitumen. The separation reagent can be recovered and used in other processes after removal and recovery of the clay. The separation reagent must be substantially diluted after being recycled and reused to reduce solvation properties.
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