초록 ▼

Discloses apparatus to perform a process to remove water and minerals from a bitumen froth output of a oil sands hot water extraction process. A bitumen froth feed stream is diluted with a solvent and supplied to a primary inclined plate separator stage, which separates the bitumen into an overflow

Discloses apparatus to perform a process to remove water and minerals from a bitumen froth output of a oil sands hot water extraction process. A bitumen froth feed stream is diluted with a solvent and supplied to a primary inclined plate separator stage, which separates the bitumen into an overflow stream providing a bitumen product output from the circuit and a bitumen depleted underflow stream. A primary cyclone state, a secondary inclined plate separator stage and a secondary cyclone stage further process the underflow stream to produce a secondary bitumen recovery product stream and a recycle stream. The secondary bitumen recovery product stream is incorporated into and becomes part of the circuit bitumen product output stream. The recycle stream is incorporated into the bitumen froth feed stream for reprocessing by the circuit.

대표청구항 ▼

What is claimed is: 1. An apparatus for separating bitumen from a bitumen feed comprising a mixture of bitumen, water and mineral, the apparatus comprising: (a) an inclined plate separator (IPS) for providing a first bitumen separation stage, the IPS having an inlet for receiving the bitumen feed i

What is claimed is: 1. An apparatus for separating bitumen from a bitumen feed comprising a mixture of bitumen, water and mineral, the apparatus comprising: (a) an inclined plate separator (IPS) for providing a first bitumen separation stage, the IPS having an inlet for receiving the bitumen feed in a hybrid emulsion phase comprising a melange of water-continuous and oil-continuous emulsions, an overflow outlet for providing a first bitumen-enriched stream separated from the hybrid emulsion phase of the bitumen feed, and an underflow outlet for providing a first bitumen-lean stream separated from the hybrid emulsion phase of the bitumen feed, the first bitumen-lean stream comprising primarily a water-continuous emulsion; (b) a first cyclone for providing a second bitumen separation stage, the first cyclone having a first cyclone inlet for receiving the first bitumen-lean stream, a first cyclone overflow outlet for providing a second bitumen-enriched stream separated from the first bitumen-lean stream, and a first cyclone underflow outlet for providing a second bitumen-lean stream separated from the first bitumen-lean stream; and (c) a recycle path for communicating the second bitumen-enriched stream for further processing upstream of the first cyclone. 2. The apparatus according to claim 1 further comprising a second cyclone for providing a third bitumen separation stage, the second cyclone having a second cyclone inlet for receiving the second bitumen-lean stream, a second cyclone overflow outlet for providing a third bitumen-enriched stream separated from the second bitumen-lean stream, and a second cyclone underflow outlet for providing a third bitumen-lean stream separated from the second bitumen-lean stream. 3. The apparatus according to claim 2 further comprising a second recycle path for communicating the third bitumen-enriched stream upstream of the second cyclone for further processing by the second cyclone. 4. The apparatus according to claim 2 further comprising a second recycle path for communicating the third bitumen-enriched stream upstream of the first cyclone for further processing by the first cyclone. 5. The apparatus according to claim 2 further comprising a second recycle path for communicating the third bitumen-enriched stream upstream of the IPS for further processing by the IPS. 6. The apparatus according to claim 2 further comprising a second recycle path for communicating the third bitumen-enriched stream to the IPS inlet for further processing by the IPS. 7. The apparatus according to claim 2 further comprising a second recycle path for recycling the third bitumen-enriched stream to the second cyclone for further processing by the second cyclone. 8. The apparatus according to claim 2 further comprising a second recycle path for recycling the third bitumen-enriched stream to the first cyclone for further processing by the first cyclone. 9. The apparatus according to claim 2 further comprising a second recycle path for recycling the third bitumen-enriched stream to the IPS for further processing by the IPS. 10. The apparatus according to claim 2 further comprising a further bitumen separation stage upstream of the second cyclone. 11. The apparatus according to claim 10 wherein the further bitumen separation stage comprises a further IPS for receiving and processing the second bitumen-enriched stream. 12. The apparatus according to claim 10 wherein the further bitumen separation stage comprises a further IPS for receiving and processing at least a portion of the second bitumen-enriched stream. 13. The apparatus according to claim 12 further comprising a diverter for selectively diverting at least a portion of the second bitumen-enriched stream between at least the recycle path and an inlet for the further bitumen separation stage. 14. The apparatus according to claim 10 further comprising a diverter for selectively diverting at least a portion of the second bitumen-enriched stream between at least the recycle path and an inlet for the further bitumen separation stage. 15. The apparatus according to claim 10 further comprising a blending region, in communication with the recycle path, for blending the second bitumen-enriched stream with a portion of the bitumen feed before the second bitumen-enriched stream is communicated to the IPS inlet. 16. The apparatus according to claim 1 wherein the recycle path is operatively configured to communicate the second bitumen-enriched stream to the inlet of the IPS. 17. The apparatus according to claim 16 further comprising a blending region, in communication with the recycle path, for blending the second bitumen-enriched stream with a portion of the bitumen feed before the second bitumen-enriched stream is communicated to the IPS inlet. 18. The apparatus according to claim 1 further comprising a diluent inlet coupled to the inlet of said IPS for diluting the bitumen feed. 19. The apparatus according to claim 18 further comprising a diluent recovery unit in communication with the first cyclone for recovering a portion of the diluent. 20. An apparatus for separating bitumen from a bitumen feed in a hybrid emulsion phase comprising a melange of water-continuous and oil-continuous emulsions, the bitumen feed comprising a mixture of bitumen, water and mineral, the apparatus comprising: (a) means for separating the hybrid emulsion phase of the bitumen feed with an inclined plate separator into a first overflow stream and a first underflow stream, the first overflow stream comprising a first bitumen-enriched stream separated from the hybrid emulsion phase and the first underflow stream comprising a first bitumen-lean stream, the first bitumen-lean stream comprising primarily a water-continuous emulsion; (b) means for processing the first underflow stream with a first cyclone to separate the first underflow stream into a second overflow stream and a second underflow stream, the second overflow stream comprising a second bitumen-enriched stream and the second underflow stream comprising a second bitumen-lean stream; and (c) means for recycling the second bitumen-enriched stream upstream of the first cyclone for further processing. 21. The apparatus according to claim 20 further comprising means for supplying the second bitumen-lean stream to a second cyclone and means for processing the second bitumen-lean stream with the second cyclone to separate the second bitumen-lean stream into a third bitumen-enriched stream and a third bitumen-lean stream. 22. The apparatus according to claim 21 further comprising means for recycling the third bitumen-enriched stream for further processing upstream of the second cyclone. 23. The apparatus according to claim 21 further comprising means for recycling the third bitumen-enriched stream for further processing upstream of the first cyclone. 24. The apparatus according to claim 21 further comprising means for recycling the third bitumen-enriched stream upstream of the first cyclone for further processing by the inclined plate separator. 25. The apparatus according to claim 20 further comprising means for diverting at least a portion of the second bitumen-enriched stream from being recycled to supply the at least a portion of the second bitumen-enriched stream to a further bitumen separation stage downstream of the first cyclone.