Bitumen recovery from oil sands tailings
US-2016090536-A1 · Mar 31, 2016 · US
US10907103B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10907103-B2 |
| Application number | US-201916378301-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 8, 2019 |
| Priority date | Apr 9, 2018 |
| Publication date | Feb 2, 2021 |
| Grant date | Feb 2, 2021 |
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A process for extracting bitumen from mined oil sand is provided, comprising: preparing an oil sand slurry comprising oil sand and water; conditioning the oil sand slurry by pumping the oil sand slurry through a hydrotransport pipeline under shear conditions that reduce the formation of water-in-bitumen emulsions in the conditioned oil sand slurry and increase the size of bitumen-air aggregates; and subjecting the conditioned oil sand slurry to gravity separation to produce a bitumen froth having enhanced bitumen recovery and reduced water-in-bitumen emulsions, a middlings layer and sand tailings.
Opening claim text (preview).
We claim: 1. A process for conditioning an oil sand slurry, comprising: determining an energy dissipation rate necessary for obtaining a desired bitumen droplet size; designing a hydrotransport pipeline comprising pipe and at least one slurry pump by determining a diameter of pipe and/or a volume of the at least one slurry pump necessary to achieve the energy dissipation rate; conditioning the oil sand slurry in the so designed hydrotransport pipeline; and introducing the conditioned oil sand slurry into a primary separation vessel wherein separate layers of primary bitumen froth, middlings and sand tailings are formed. 2. The process as set forth in claim 1 , further comprising treating the primary bitumen froth with a diluent to produce a diluted bitumen product having reduced solids and/or reduced water. 3. The process as set forth in claim 2 , wherein the diluent is naphtha. 4. The process as set forth in claim 3 , wherein the naphtha diluted bitumen froth is pumped to an inclined plate settler or a scroll centrifuge for removal of solids and water from the naphtha diluted bitumen froth. 5. The process as set forth in claim 4 , wherein the solids and water reduced naphtha diluted bitumen froth is further pumped to a disc centrifuge where further solids and water are removed to form the diluted bitumen product.
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