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US4776949A Expired / Lapsed US ⏱️ 0.0 years remaining

Recycle of secondary froth in the hot water process for extracting bitumen from tar sand

Assignee: Gulf Canada Ltd
•
Filing: 1985-12-05
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Granted: 1988-10-11
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Expires: 2005-12-05
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Abstract

Abstract Froth, produced by induced air flotation in the hot water process circuit for extracting bitumen from tar sand, is recycled and added to the fresh slurry being introduced to the primary separation vessel. An increase in bitumen recovered as primary froth from the circuit is produced.

Inventors

  • 👤 Antony H. S. Leung
  • 👤 Teddy K. Kwong

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 07:26
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/047

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 168 words
In the hot water process for extracting bitumen from tar sand, wherein, in a conditioning zone, the tar sand is mixed with hot water and process aid and agitated to form a slurry and condition it, oversize material is removed from the slurry, the conditioned slurry is diluted with hot water and retained in a primary separation vessel under quiescent conditions to produce an overflow stream of primary froth and an underflow stream of tailings, a bitumen-depleted stream is withdrawn from the primary separation vessel and is subjected to induced air flotation to produce an overflow stream of secondary froth and an underflow stream of tailings, the improvement comprising: recycling at least part of the secondary froth to that portion of the hot water process which is downstream of the conditioning zone and upstream of the primary separation vessel to join and mix with the feed stream moving to the primary separation vessel; and thereafter retaining said feed stream in said primary separation vessel to produce primary froth.
Claim 2
Dependent Claim 168 words
In the hot water process for extracting bitumen from tar sand, wherein, in a conditioning zone, the tar sand is mixed with hot water and process aid and agitated to form a slurry and condition it, oversize material is removed from the slurry, the conditioned slurry is diluted with hot water and retained in a primary separation vessel under quiescent conditions to produce an overflow stream of primary froth and an underflow stream of tailings, a bitumen-depleted stream is withdrawn from the primary separation vessel and is subjected to induced air flotation to produce an overflow stream of secondary froth and an underflow stream of tailings, the improvement comprising: recycling at least part of the secondary froth to that portion of the hot water process which is downstream of the conditioning zone and upstream of the primary separation vessel to join and mix with the feed stream moving to the primary separation vessel; and thereafter retaining said feed stream in said primary separation vessel to produce primary froth.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein the withdrawn bitumen-depleted stream is middlings from the primary separation vessel.

References Cited (Backward Citations)

US3526585A Cited
US3607720A Cited
CA1011273A Cited
CA1012083A Cited
CA1055868A Cited
US4533459A Cited
US4462892A Cited
US4474616A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1991-10-11 1992-04-11 1992-10-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1995-10-11 1996-04-11 1996-10-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1999-10-11 2000-04-11 2000-10-11 $7700.00 Window Closed / Lapsed

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