US4040958A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for separating solids from high-boiling hydrocarbons in a plurality of separation stages
Assignee: GEA Group AG
•
Filing: 1976-01-26
•
Granted: 1977-08-09
•
Expires: 1996-01-26
Abstract
Abstract Solids are separated from solids-containing, high-boiling hydrocarbons by mixing a lower-boiling liquid diluent with the solids-containing, high-boiling hydrocarbons, clarifying the mixture to separate same into a solid-enriched phase and a low-solids liquid phase, separating the high-boiling hydrocarbons from the low-solids phase by distillation, and recovering and reusing the diluent. The high-boiling hydrocarbons can be heavy oil or heavy tar from the thermal treatment of hard coal, brown coal, tar sands, oil shale or the like.
Inventors
- 👤 Roland Rammler
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 13:08
CPC Classifications
C; C10; C10G; C10G31/00; B; B01; B01D; B01D11/00; B01D11/02; B03; B03B; B03B9/00; C10G21/00; C10G21/003
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
172 words
Process of separating solids from solids-containing, high-boiling hydrocarbons in two or more separation stages, each separation stage comprising a mixing zone and downstream from said mixing zone a separation zone, said process comprising (a) withdrawing from each separation zone a low-solids liquid phase and a solids-enriched phase and feeding said solids-enriched phase from each separation zone to the mixing zone of the following stage; (b) feeding said solids-containing, high-boiling hydrocarbons together with a low-boiling liquid hydrocarbon diluent and the low-solids liquid phase withdrawn from the separation zone of the second separation stage to the mixing zone of the first separation stage, said diluent containing at least one component selected from the group consisting of medium oil, light oil or gasoline, (c) feeding the low-solids liquid phase from said first separation stage to a distillation zone and recovering said low-boiling diluent therefrom, (d) feeding the low-solids liquid phase of each stage following said first stage to the mixing zone of the preceding stage and (e) recovering solids-free, high-boiling hydrocarbons from said distillation zone.
Claim 2
Dependent Claim
172 words
Process of separating solids from solids-containing, high-boiling hydrocarbons in two or more separation stages, each separation stage comprising a mixing zone and downstream from said mixing zone a separation zone, said process comprising (a) withdrawing from each separation zone a low-solids liquid phase and a solids-enriched phase and feeding said solids-enriched phase from each separation zone to the mixing zone of the following stage; (b) feeding said solids-containing, high-boiling hydrocarbons together with a low-boiling liquid hydrocarbon diluent and the low-solids liquid phase withdrawn from the separation zone of the second separation stage to the mixing zone of the first separation stage, said diluent containing at least one component selected from the group consisting of medium oil, light oil or gasoline, (c) feeding the low-solids liquid phase from said first separation stage to a distillation zone and recovering said low-boiling diluent therefrom, (d) feeding the low-solids liquid phase of each stage following said first stage to the mixing zone of the preceding stage and (e) recovering solids-free, high-boiling hydrocarbons from said distillation zone.
Claim 3
Dependent Claim
14 words
Process of claim 1 wherein the high-boiling hydrocarbons are dissolved in said liquid diluent.
Claim 4
Dependent Claim
30 words
Process of claim 1 wherein the high-boiling hydrocarbons are heavy oil or heavy tar from the thermal treatment of hard coal, brown coal, tar sands, oil shale or bitumen-containing materials.
Claim 5
Dependent Claim
61 words
Process of claim 1 wherein the dust-containing high-boiling hydrocarbons are mixed in a first separation stage with a diluent which contains high-boiling hydrocarbons, the high-solids phase separated therefrom is mixed once more with diluent in at least one subsequent separating stage, and the phase which is substantially free from solids includes said diluent and is fed to the preceding separation stage.
Claim 6
Dependent Claim
23 words
Process of claim 4 wherein diluent distilled from the phase that is substantially free from solids is fed to the last separation stage.
Claim 7
Dependent Claim
32 words
Process of claim 1 wherein the high-solids phase is separated in at least one of the separation stages by sedimentation, centrifuging or filtering from the phase which is substantially free from solids.
Claim 8
Dependent Claim
30 words
Process of claim 1 wherein the high-solids phase from the last separation stage is dried, the escaping vapors are condensed, and the condensate is recycled to the last separation stage.
Claim 9
Dependent Claim
18 words
Process of claim 1 wherein the solids-containing, high-boiling hydrocarbons have a solids content of about 5-70% by weight.
References Cited (Backward Citations)
US2235639A
Cited
US2914518A
Cited
US3468789A
Cited
US3396100A
Cited
US3696021A
Cited
US3684699A
Cited
US3878090A
Cited
US3900389A
Cited
US3974073A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-08-08 | 1981-02-07 | 1981-08-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-08 | 1985-02-07 | 1985-08-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-08 | 1989-02-07 | 1989-08-09 | $7700.00 | Window Closed / Lapsed |