Process for extracting bitumen from tar sands

Claim 2

A process for recovering bitumen from tar sands wherein bitumen is extracted from the tar sands with a solvent which process comprises contacting the bitumen solution comprising said solvent, bitumen and sand fines with water containing about 0.01 to about 0.10 weight percent of a cationic surfactant to effect the removal of said sand fines from said bitumen solution, recovering the resulting bitumen solution thereafter and recovering bitumen from said bitumen solution.

Claim 3

A process in accordance with claim 1 wherein said cationic surfactant comprises 80 percent methyldodecylbenzyl trimethylammonium chloride and 20 percent methyldodecylxylylene-bis-(trimethylammonium chloride).

Claim 4

A process in accordance with claim 1 wherein said solvent is an aromatic hydrocarbon solvent.

Claim 5

A process for recovering bitumen from tar sands comprising the steps of: (a) mixing the tar sands with an extractive solvent, (b) allowing the mixture of step (a) to settle into a fine sand-bitumen solvent phase and a coarse sand phase, (c) removing the fine sand-bitumen solvent phase, (d) contacting said fine sand-bitumen solvent phase with water containing a cationic surfactant wherein the amount of said cationic surfactant present in the water is the range of about 0.01 to about 0.10 weight percent and allowing the mixture to settle into a solvent phase, an interface zone where the fines collect, and an aqueous phase, and (e) removing the solvent phase and separating said phase into solvent and bitumen product.

Claim 6

A process for recovering bitumen from tar sands comprising the steps of: (a) mixing the tar sands with an extractive solvent, (b) allowing the mixture of step (a) to settle into a fine sand-bitumen solvent phase and a coarse sand phase, (c) removing the fine sand-bitumen solvent phase, (d) contacting said fine sand-bitumen solvent phase with water containing a cationic surfactant wherein the amount of said cationic surfactant present in the water is the range of about 0.01 to about 0.10 weight percent and allowing the mixture to settle into a solvent phase, an interface zone where the fines collect, and an aqueous phase, and (e) removing the solvent phase and separating said phase into solvent and bitumen product.

Claim 7

A process in accordance with claim 4 which further comprises diluting the solvent phase to be separated into solvent and bitumen product prior to said separation with a high boiling solvent in order to reduce the viscosity of the bitumen during solvent recovery.

Claim 8

A process in accordance with claim 4 wherein said solvent is an aromatic hydrocarbon solvent.

Claim 9

A process in accordance with claim 6 wherein said aromatic hydrocarbon solvent is toluene and the cationic surfactant comprises 80 percent methyldodecylbenzyl trimethylammonium chloride and 20 percent methyldodecylxylene-bis-(trimethylammonium chloride).