US4628391A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for dispersing two phases in liquid-liquid extraction
Assignee: Outokumpu Oyj
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Filing: 1984-05-14
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Granted: 1986-12-09
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Expires: 2004-05-14
Abstract
Abstract The present invention concerns a way to achieve in liquid-liquid extraction in the step of dispersing two different solution phases the transformation of the desired phase, which may also be the phase with smaller volume, to become the continuous phase, with the aid of a primarily vertical circulation flow. The invention also concerns an apparatus serving this purpose, a circulation dispersion contactor, in which the smooth circulation of the dispersion is accomplished by the aid of a radial pump turbine designed for this particular purpose, or of an axial propeller, and of distribution/guide rings on the periphery of the contactor.
Inventors
- 👤 Bror G. Nyman
- 👤 Stig-Erik Hultholm
- 👤 Launo L. Lilja
- 👤 Valto J. Makitalo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 23:21
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/04; B01D11/0446; B01D11/0457; B01F; B01F27/00; B01F27/05; B01F27/11; B01F27/19; B01F27/192; B01F23/00; B01F23/40; B01F23/43; B01F27/80; B01F27/86
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
127 words
A process, for mixing a light liquid phase and a heavy liquid phase in liquid-liquid extraction with each other to produce a good dispersion, comprising maintaining the light phase continuous and dispersing in the heavy phase in the light phase, said continuous light phase having a volume smaller than or at most equal to the volume of the dispersed heavy phase, by causing a substantially vertical circulation flow to take place in the dispersing volume, and including initiating said circulation flow in the said light phase; and wherein the dispersion is circulated in the dispersion volume through several cycles before it is removed from the dispersion volume and the circulating time of the dispersion is shorter than the separating time of the solution phases in the dispersion.
Claim 2
Dependent Claim
127 words
A process, for mixing a light liquid phase and a heavy liquid phase in liquid-liquid extraction with each other to produce a good dispersion, comprising maintaining the light phase continuous and dispersing in the heavy phase in the light phase, said continuous light phase having a volume smaller than or at most equal to the volume of the dispersed heavy phase, by causing a substantially vertical circulation flow to take place in the dispersing volume, and including initiating said circulation flow in the said light phase; and wherein the dispersion is circulated in the dispersion volume through several cycles before it is removed from the dispersion volume and the circulating time of the dispersion is shorter than the separating time of the solution phases in the dispersion.
Claim 3
Dependent Claim
138 words
A process for mixing a light liquid phase and a heavy liquid phase in liquid-liquid extraction to produce a good dispersion of the heavy phase as droplets while maintaining the light phase continuous even though the light phase has a volume less than or at most equal to the volume of the heavy phase comprising feeding a heavy liquid phase and a light liquid phase into a circulation dispersion contactor so that the light phase is above the heavy phase, causing rotatable pumping means to rotate in the light phase, thereby causing motion of the light phase, which motion disperses the heavy phase as droplets in the ligh phase and continuing rotation of said pumping means to maintain the dispersion of the heavy phase in the light phase while withdrawing the mixed phase from the circulation dispersion contactor.
Claim 4
Dependent Claim
138 words
A process for mixing a light liquid phase and a heavy liquid phase in liquid-liquid extraction to produce a good dispersion of the heavy phase as droplets while maintaining the light phase continuous even though the light phase has a volume less than or at most equal to the volume of the heavy phase comprising feeding a heavy liquid phase and a light liquid phase into a circulation dispersion contactor so that the light phase is above the heavy phase, causing rotatable pumping means to rotate in the light phase, thereby causing motion of the light phase, which motion disperses the heavy phase as droplets in the ligh phase and continuing rotation of said pumping means to maintain the dispersion of the heavy phase in the light phase while withdrawing the mixed phase from the circulation dispersion contactor.
Claim 5
Dependent Claim
39 words
The process of claim 2 and including feeding the heavy and light phases into the contactor from below the contactor to a zone adjacent said pumping means and withdrawing the mixed phases from the contactor above the pumping means.
References Cited (Backward Citations)
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-12-08 | 1990-06-09 | 1990-12-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-12-08 | 1994-06-09 | 1994-12-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-12-08 | 1998-06-09 | 1998-12-09 | $7700.00 | Window Closed / Lapsed |