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US5213976A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for obtaining a polyhydroxyalkanoate from the cell material of a microogranism

Assignee: PCD Polymere GmbH
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Filing: 1991-09-17
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Granted: 1993-05-25
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Expires: 2011-09-17
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Abstract

Abstract Process for extracting polyhydroxyalkanoates from the cell material of microorganisms by adding an organic solvent for the polyhydroxyalkanoate which is immiscible with water and which has a boiling point of below 100° C., and, if appropriate, by adding water; stirring the resulting extraction mixture, if appropriate with refluxing; separating off the aqueous phase which contains the cell material in undissolved form from the organic phase; and injecting the organic phase into hot water, causing the dissolved polyhydroxyalkanoate to precipitate and the organic solvent to evaporate, and also isolating the precipitated polyhydroxyalkanoate flocs.

Inventors

  • 👤 Wilfried Blauhut
  • 👤 Wolfgang Gierlinger
  • 👤 Friedrich Strempfl

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 13:24
CPC Classifications
C; C12; C12P; C12P7/00; C12P7/62; C12P7/625; Y; Y10; Y10S; Y10S435/00; Y10S435/8215; Y10S435/822; Y10S435/829

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 191 words
A process for obtaining a polyhydroxyalkanoate, synthesized intracellularly by a microorganism, from the cell material of a fermented, aqueous cell suspension, comprising: removing at least part of the fermentation solution, or at least part of the water contained in the fermentation solution, from the cell suspension, treating the cell material with an organic solvent to extract the polyhydroxyalkanoate from the cell material, which solvent is immiscible with water and which has a boiling point of less than 100° C., with or without the addition of water, stirring the resulting extraction mixture at a temperature of from room temperature to the boiling point of the organic solvent, allowing the mixture to settle, with or without centrifugation to obtain an aqueous phase and an organic phase, separating the organic phase which contains the polyhydroxyalkanoate in dissolved form from the aqueous phase which contains the cell residues in undissolved form, injecting the organic phase into hot water at a temperature which is higher than the boiling point of the organic solvent, thereby causing the organic solvent to evaporate and the polyhydroxyalkanoate to precipitate in the water in flocs, and isolating the precipitated polyhydroxyalkanoate flocs.
Claim 2
Dependent Claim 191 words
A process for obtaining a polyhydroxyalkanoate, synthesized intracellularly by a microorganism, from the cell material of a fermented, aqueous cell suspension, comprising: removing at least part of the fermentation solution, or at least part of the water contained in the fermentation solution, from the cell suspension, treating the cell material with an organic solvent to extract the polyhydroxyalkanoate from the cell material, which solvent is immiscible with water and which has a boiling point of less than 100° C., with or without the addition of water, stirring the resulting extraction mixture at a temperature of from room temperature to the boiling point of the organic solvent, allowing the mixture to settle, with or without centrifugation to obtain an aqueous phase and an organic phase, separating the organic phase which contains the polyhydroxyalkanoate in dissolved form from the aqueous phase which contains the cell residues in undissolved form, injecting the organic phase into hot water at a temperature which is higher than the boiling point of the organic solvent, thereby causing the organic solvent to evaporate and the polyhydroxyalkanoate to precipitate in the water in flocs, and isolating the precipitated polyhydroxyalkanoate flocs.
Claim 3
Dependent Claim 17 words
The process according to claim 1, wherein the polyhydroxyalkanoate is a homopolymer or copolymer of poly-D(-)-3-hydroxybutyric acid.
Claim 4
Dependent Claim 23 words
The process according to claim 1, wherein the at least part of the fermentation solution is removed from the cell suspension by centrifugation.
Claim 5
Dependent Claim 43 words
The process according to claim 1, wherein the cell material is treated with an amount of organic solvent and an amount of water so that the ratio by weight of cell material relative to the cell dry weight:water:solvent is from 2:3:20 to 1:5:50.
Claim 6
Dependent Claim 14 words
The process according to claim 1, wherein the extraction mixture is centrifuged after stirring.
Claim 7
Dependent Claim 23 words
The process according to claim 1, wherein the organic phase is injected into hot water with the aid of steam as a propellant.
Claim 8
Dependent Claim 21 words
The process according to claim 1, wherein the precipitated polyhydroxyalkanoate is stirred in the hot water for 20 to 40 minutes.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-05-24 1996-11-23 1997-05-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-05-24 2000-11-23 2001-05-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-05-24 2004-11-23 2005-05-25 $7700.00 Window Closed / Lapsed

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