Patent US4824570A successfully refreshed from Google Patents.
US4824570A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for the extraction of constituents by a supercritical fluid or pressurized liquid
Assignee: Commissariat à l'Énergie Atomique et Aux Énergies Alternatives
•
Filing: 1986-09-02
•
Granted: 1989-04-25
•
Expires: 2006-09-02
Abstract
Abstract PCT No. PCT/FR86/00295 Sec. 371 Date Apr. 2, 1987 Sec. 102(e) Date Apr. 2, 1987 PCT Filed Sep. 2, 1986 PCT Pub. No. WO87/01299 PCT Pub. Date Mar. 12, 1987.An apparatus for the extraction of constituents present in a substance by means of an extraction fluid constituted by a supercritical fluid or a pressurized liquid. According to this apparatus, in an exterior (3) contacting takes place between the substance and the extraction fluid in order to dissolve the constituents in fluid. The fluid leaving the extractor is then treated to separate the extracted constituents. The fluid is expanded at a pressure p1. Firstly, the less volatile constituents are separated in a liquid-gas separator (41), the separated gas is then liquefied in gas separator-liquefier (13) and the thus liquefied gas is rectified in column (19) to concentrate the extracted constituents in the liquid phase. The extraction fluid can be carbon dioxide gas.
Inventors
- 👤 Louis Bethuel
- 👤 Maurice Carles
- 👤 Roger Neige
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 12:16
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/04; B01D11/0403; B01D11/0407; B01D11/02; B01D11/0203
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
170 words
Apparatus for the extraction of at least one of the constituents present in a substance by means of an extraction fluid constituted by a supercritical fluid or a pressurized liquid, comprising an extractor (3) within which can be placed said substance, means (9) for circulating the extraction fluid in said extractor under pressure p and temperature T conditions adequate for dissolving the constituent or constituents of the substance in said fluid and a discharge pipe (7) for the extraction fluid leaving the extractor equipped with a relief valve (5) wherein said pipe (7) is connected to the lower part of a gas separator-liquefier (13) provided with cooling means (15, 17) linked by its upper part with a vertical column (19) surmounted by a condenser (21), said gas separator-liquefier (13) being provided in its lower part with means (14) for withdrawing a liquefied phase present in said separator-liquefier and in that a gas-liquid separator (41) is interposed on the gas circuit between the relief valve (5) and the gas separator-liquefier (13).
Claim 2
Dependent Claim
170 words
Apparatus for the extraction of at least one of the constituents present in a substance by means of an extraction fluid constituted by a supercritical fluid or a pressurized liquid, comprising an extractor (3) within which can be placed said substance, means (9) for circulating the extraction fluid in said extractor under pressure p and temperature T conditions adequate for dissolving the constituent or constituents of the substance in said fluid and a discharge pipe (7) for the extraction fluid leaving the extractor equipped with a relief valve (5) wherein said pipe (7) is connected to the lower part of a gas separator-liquefier (13) provided with cooling means (15, 17) linked by its upper part with a vertical column (19) surmounted by a condenser (21), said gas separator-liquefier (13) being provided in its lower part with means (14) for withdrawing a liquefied phase present in said separator-liquefier and in that a gas-liquid separator (41) is interposed on the gas circuit between the relief valve (5) and the gas separator-liquefier (13).
Claim 3
Dependent Claim
32 words
Apparatus according to claim 1, wherein the cooling means (15, 17) of said gas separator-liquefier comprises means for cooling the lower part thereof to a temperature below that of its upper part.
Claim 4
Dependent Claim
38 words
Apparatus according to claims 1 or 2, characterized in that condenser (2) located at the upper end of column (19) is surmounted by a heat exchanger (21) for raising the gas leaving the condenser to a higher temperature.
Claim 5
Dependent Claim
14 words
Apparatus according to claim 1, wherein the gas-liquid separator (41) is a cyclone separator.
Claim 6
Dependent Claim
115 words
Apparatus according to claim 1 which comprises: a closed main circuit having in series the extractor (3), said relief valve (5), a gas-liquid separator (41) and means (43, 45, 47) for recycling the gas leaving said separator (41) into said extractor (3) at the extraction temperature T and pressure p and a gas separator-liquefier (13) linked by its upper part with a vertical column (19) surmounted by a condenser (21), said gas separator-liquefier (13) being branched on to the main circuit be means of a pipe (51) having a valve (53) issuing into said main circuit between the gas-liquid separator (41) and said means (43, 45, 47) for recycling the gas into the extractor (3).
Claim 7
Dependent Claim
110 words
Apparatus according to claim 1 which comprises: a closed main circuit having in series the extractor (3), said relief valve (5), the gas-liquid separator (41) and means (43, 45,) said extractor (3) at extraction temperature T and pressure p, a gas separator-liquefier (13) linked by its upper part with a vertical column (19) surmounted by a condenser (21), means for continuously discharging into a container (61) the liquid phase separated in said gas-liquid separator (41) and means for connecting the upper part of the container (61) to the gas liquefier-separator (13) in order to treat therein the gas able to pass from the liquid-gas separator (41) into the container (61).
Claim 8
Dependent Claim
131 words
Apparatus according to claim 1 which comprises: a closed main circuit having in series the extractor (3), said relief valve (5), a gas-liquid separator (41), a gas separator-liquefier (13) linked by its upper part with a vertical column (19) surmounted by a condenser (21) and means (43, 45, 47) for recycling the gas leaving said condenser (21) into the said extractor (3) at the extraction temperature T and pressure p, means (14) for discontinuously sampling the liquid phase present in the gas separator-liquefier (13), means (71) for evaporating the sampled liquid phase and means (75, 77) for recycling the gas separated during the evaporation of the liquid phase sampled in the main circuit between the condenser (21) and the means (43, 45, 47) for recycling the gas into the extractor (3).
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) | 1992-04-24 | 1992-10-24 | 1993-04-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-04-24 | 1996-10-24 | 1997-04-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-04-24 | 2000-10-24 | 2001-04-25 | $7700.00 | Window Closed / Lapsed |