US4116809A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Deaerator circuit for bitumen froth
Assignee: Ministry of Natural Resources and Wildlife
•
Filing: 1976-12-02
•
Granted: 1978-09-26
•
Expires: 1996-12-02
Abstract
Abstract Bitumen froth streamsfrom the primary separation vessel and secondary flotation cells are gravity transferred into one or more columns and heated and deaerated therein by passing them countercurrent to steam. The heated deaerated froth is then pumped with centrifugal pump means to the froth treatment circuit. By deaerating and heating before pumping, the froth is converted from a form difficult to pump to one which is relatively easy to pump.
Inventors
- 👤 Thaddeus Eugene Kizior
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 09:52
CPC Classifications
B; B03; B03D; B03D1/00; B03D1/08; B01; B01D; B01D19/00; B01D19/0068; C; C10; C10G; C10G1/00; C10G1/04; C10G1/047
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
157 words
In the hot water extraction process for treating tar sand wherein primary and secondary froth streams are produced by a primary separation vessel and a secondary flotation cell, said streams comprising mixtures of bitumen, water and solids, and the streams are transferred to a froth treatment circuit for recovering the bitumen, the improvement which comprises: directly feeding the secondary froth stream by gravity from a secondary flotation cell to a first deaerator tower and heating and deaerating said stream by passing it countercurrently to steam through said tower; conveying the deaerated secondary froth stream to a second deaerator tower; directly feeding the primary froth stream by gravity from a primary separation vessel to the second deaerator tower; passing said streams countercurrently to steam through said second tower to heat and deaerate them to provide a pumpable deaerated bitumen, water and solids product; and pumping the product with one or more centrifugal pumps to the froth treatment circuit.
Claim 2
Dependent Claim
157 words
In the hot water extraction process for treating tar sand wherein primary and secondary froth streams are produced by a primary separation vessel and a secondary flotation cell, said streams comprising mixtures of bitumen, water and solids, and the streams are transferred to a froth treatment circuit for recovering the bitumen, the improvement which comprises: directly feeding the secondary froth stream by gravity from a secondary flotation cell to a first deaerator tower and heating and deaerating said stream by passing it countercurrently to steam through said tower; conveying the deaerated secondary froth stream to a second deaerator tower; directly feeding the primary froth stream by gravity from a primary separation vessel to the second deaerator tower; passing said streams countercurrently to steam through said second tower to heat and deaerate them to provide a pumpable deaerated bitumen, water and solids product; and pumping the product with one or more centrifugal pumps to the froth treatment circuit.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-09-25 | 1982-03-27 | 1982-09-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-25 | 1986-03-27 | 1986-09-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-25 | 1990-03-27 | 1990-09-26 | $7700.00 | Window Closed / Lapsed |