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US4828702A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for separating a solid substance from a liquid mixture of substances

Assignee: Fried Krupp AG
•
Filing: 1987-08-25
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Granted: 1989-05-09
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Expires: 2007-08-25
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Abstract

Abstract Process for separating solid substances from liquid mixtures of substances, wherein the liquid substances contained in the mixture are separated from the solid substances by countercurrent extraction with a solvent which, during the extraction process, is in a liquid or supercritical state and which, under standard conditions, is gaseous. The solvent is fed to a cylindrical extraction chamber at the lowest point of the extraction chamber. The solvent leaves the nozzles with a Reynold's number of 40,000 and flows upward in the extraction chamber with a Reynold's number of 2,700 to 8,000.

Inventors

  • 👤 Hubert Coenen
  • 👤 Rainer Hagen
  • 👤 Klaus Reimann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 21:49
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/02; B01D11/0203

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 252 words
Process for recovering a powder by separating a liquid mixture of substances comprised of a dissolved solid substance and liquid substances, in which the liquid substances are separated from the solid substance by countercurrent extraction in an extraction chamber with a solvent to form a solvent phase which is loaded with the liquid substances and an extraction phase comprising said solid substance and solvent, the solvent, during the countercurrent extraction, is in a liquid or supercritical state and under standard conditions, is gaseous, the solvent phase which is loaded with the liquid substances is removed from the extraction chamber, the solvent phase subsequently is resolved by pressure reduction and/or temperature change into its components to recover gaseous solvent, the recovered gaseous solvent is returned into the extraction chamber, and the solid substance is recovered from said extraction phase in powder form, said process comprising (a) feeding the solvent to a cylindrical extraction chamber at the lowest point of the extraction chamber through nozzles, the extraction chamber having a diameter-to-height ratio of 1:5 to 1:10 and not having any internal components, the nozzles being in the form of bores and forming an angle of 0 to 60° with the axis of the extraction chamber, and (b) controlling the flow of the solvent through the extraction chamber by selecting the number and bore-width of the nozzles so that the solvent leaves the nozzles with a Reynolds' number of >40,000 and flows upwards in the extraction chamber with a Reynolds' number of 2,700 to 8,000.
Claim 2
Dependent Claim 252 words
Process for recovering a powder by separating a liquid mixture of substances comprised of a dissolved solid substance and liquid substances, in which the liquid substances are separated from the solid substance by countercurrent extraction in an extraction chamber with a solvent to form a solvent phase which is loaded with the liquid substances and an extraction phase comprising said solid substance and solvent, the solvent, during the countercurrent extraction, is in a liquid or supercritical state and under standard conditions, is gaseous, the solvent phase which is loaded with the liquid substances is removed from the extraction chamber, the solvent phase subsequently is resolved by pressure reduction and/or temperature change into its components to recover gaseous solvent, the recovered gaseous solvent is returned into the extraction chamber, and the solid substance is recovered from said extraction phase in powder form, said process comprising (a) feeding the solvent to a cylindrical extraction chamber at the lowest point of the extraction chamber through nozzles, the extraction chamber having a diameter-to-height ratio of 1:5 to 1:10 and not having any internal components, the nozzles being in the form of bores and forming an angle of 0 to 60° with the axis of the extraction chamber, and (b) controlling the flow of the solvent through the extraction chamber by selecting the number and bore-width of the nozzles so that the solvent leaves the nozzles with a Reynolds' number of >40,000 and flows upwards in the extraction chamber with a Reynolds' number of 2,700 to 8,000.
Claim 3
Dependent Claim 22 words
Process in accordance with Claim 1, wherein the liquid mixture contains 5 to 75% by weight solids dissolved in the liquid mixture.
Claim 4
Dependent Claim 23 words
Process in accordance with claim 1, wherein the liquid mixture of substances comprises, by weight, 50 to 70% lecithin and remainder vegetable oil.
Claim 5
Dependent Claim 31 words
Process according to claim 1, wherein the mass flow of the solvent, in relation to the cross-sectional area of the extraction chamber, is about 140 to about 170 kg/m 2 ×h.

References Cited (Backward Citations)

CA642370A Cited
US2364892A Cited
US3227649A Cited
US4367178A Cited
US4560513A Cited
US4491565A Cited
US4683063A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-05-08 1992-11-07 1993-05-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-05-08 1996-11-07 1997-05-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-05-08 2000-11-07 2001-05-09 $7700.00 Window Closed / Lapsed

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