Patent US4698303A successfully refreshed from Google Patents.
US4698303A
Expired / Lapsed
US
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Production of lactic acid by continuous fermentation using an inexpensive raw material and a simplified method of lactic acid purification
Assignee: Golden Technologies Co Inc
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Filing: 1986-03-27
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Granted: 1987-10-06
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Expires: 2006-03-27
Abstract
Abstract The invention provides a method for producing lactic acid by continuous fermentation utilizing particular methods of media pretreatment, cell-recycle fermentation, fermentation broth acidification, and lactic acid separation.
Inventors
- 👤 Richard B. Bailey
- 👤 Dilip K. Joshi
- 👤 Stephen L. Michaels
- 👤 Richard A. Wisdom
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 14:05
CPC Classifications
C; C12; C12P; C12P7/00; C12P7/40; C12P7/56; A; A23; A23C; A23C21/00; A23C21/02; A23C21/023; Y; Y10; Y10S; Y10S435/00; Y10S435/813; Y10S435/8215; Y10S435/822; Y10S435/853; Y10S435/854; Y10S435/856; Y10S435/885
Claims Analysis
Total Claims: 31
Claim 1
Independent Claim
287 words
A process for producing lactic acid from whey comprising the steps of: (a) providing a whey composition at an acidic pH from which a substantial portion of proteins having a molecular weight over 10,000 have been removed; (b) treating said composition with a protease at a temperature in the range of 40° C. to 65° C. for a period sufficient to degrade proteins to smaller peptides and amino acids, said smaller peptides and amino acids characterized as being nonpercipitable when subjected to heat-sterilization, increased salt concentration or contact with organic solvents; (c) fermenting the composition resulting from step (b) with a lactic acid or lactic acid salt-producing microorganism in a fermentation zone; (d) continuously removing a product-containing broth from said zone, removing cells of said microorganism from said broth to form a cell-free product-containing stream and recycling said cells to said zone; (e) contacting said cell-free product-containing stream at an acidic pH with a water-immiscible liquid consisting essentially of trialkyl tertiary amines of at least 24 carbon atoms and a water-immiscible organic solvent for a sufficient time and temperature, whereby lactic acid and lactic acid salt are extracted from said stream into a water-immiscible phase, said liquid characterized by a distribution coefficient in excess of 1.0 for lactic acid and lactic acid salt in said liquid versus water; (f) separating said water-immiscible phase from the mixture formed in step (e); (g) contacting said water-immiscible liquid from step (f) with a material selected from the group consisting of aqueous ammonium hydroxide, solid alkalis, solid alkaline earth compounds, and aqueous non-homogenous suspensions of solid alkalis or solid alkaline earth compounds for a sufficient time and temperature, whereby lactic acid and lactic acid salt are removed from said water-immiscible phase.
Claim 2
Dependent Claim
287 words
A process for producing lactic acid from whey comprising the steps of: (a) providing a whey composition at an acidic pH from which a substantial portion of proteins having a molecular weight over 10,000 have been removed; (b) treating said composition with a protease at a temperature in the range of 40° C. to 65° C. for a period sufficient to degrade proteins to smaller peptides and amino acids, said smaller peptides and amino acids characterized as being nonpercipitable when subjected to heat-sterilization, increased salt concentration or contact with organic solvents; (c) fermenting the composition resulting from step (b) with a lactic acid or lactic acid salt-producing microorganism in a fermentation zone; (d) continuously removing a product-containing broth from said zone, removing cells of said microorganism from said broth to form a cell-free product-containing stream and recycling said cells to said zone; (e) contacting said cell-free product-containing stream at an acidic pH with a water-immiscible liquid consisting essentially of trialkyl tertiary amines of at least 24 carbon atoms and a water-immiscible organic solvent for a sufficient time and temperature, whereby lactic acid and lactic acid salt are extracted from said stream into a water-immiscible phase, said liquid characterized by a distribution coefficient in excess of 1.0 for lactic acid and lactic acid salt in said liquid versus water; (f) separating said water-immiscible phase from the mixture formed in step (e); (g) contacting said water-immiscible liquid from step (f) with a material selected from the group consisting of aqueous ammonium hydroxide, solid alkalis, solid alkaline earth compounds, and aqueous non-homogenous suspensions of solid alkalis or solid alkaline earth compounds for a sufficient time and temperature, whereby lactic acid and lactic acid salt are removed from said water-immiscible phase.
Claim 3
Dependent Claim
279 words
A process for producing lactic acid from whey comprising the steps of: (a) providing a whey composition at an acidic pH from which a substantial portion of proteins having a molecular weight over 10,000 have been removed; (b) treating said composition with a protease at a temperature in the range of 40° C. to 65° C. for a period sufficient to degrade proteins to smaller peptides and amino acids, said smaller peptides and amino acids characterized as being nonprecipitable when subject to heat-sterilization, increased salt concentration or contact with organic solvents; (c) fermenting the composition resulting from step (b) with a lactic acid or lactic acid salt-producing microorganism in a fermentation zone; (d) removing a product-containing broth from said zone, removing cells of said microorganism from said broth to form a cell-free product-containing stream; (e) contacting said cell-free product-containing stream at an acidic pH with a water-immiscible liquid consisting essentially of trialkyl tertiary amines of at least 24 carbon atoms and a water-immiscible organic solvent for a sufficient time and temperature, whereby lactic acid and lactic acid salt are extracted from said stream into a water-immiscible phase, said liquid characterized by a distribution coefficient in excess of 1.0 for lactic acid and lactic acid salt in said liquid versus water; (f) separating said water-immiscible phase from the mixture formed in step (e); (g) contacting said water-immiscible liquid from step (f) with a material selected from the group consisting of aqueous ammonium hydroxide, solid alkalis, solid alkaline earth compounds, and aqueous non-homogenous suspensions of solid alkalis or solid alkaline earth compounds for a sufficient time and temperature, whereby lactic acid and lactic acid salt are removed from said water-immiscible phase.
Claim 4
Dependent Claim
279 words
A process for producing lactic acid from whey comprising the steps of: (a) providing a whey composition at an acidic pH from which a substantial portion of proteins having a molecular weight over 10,000 have been removed; (b) treating said composition with a protease at a temperature in the range of 40° C. to 65° C. for a period sufficient to degrade proteins to smaller peptides and amino acids, said smaller peptides and amino acids characterized as being nonprecipitable when subject to heat-sterilization, increased salt concentration or contact with organic solvents; (c) fermenting the composition resulting from step (b) with a lactic acid or lactic acid salt-producing microorganism in a fermentation zone; (d) removing a product-containing broth from said zone, removing cells of said microorganism from said broth to form a cell-free product-containing stream; (e) contacting said cell-free product-containing stream at an acidic pH with a water-immiscible liquid consisting essentially of trialkyl tertiary amines of at least 24 carbon atoms and a water-immiscible organic solvent for a sufficient time and temperature, whereby lactic acid and lactic acid salt are extracted from said stream into a water-immiscible phase, said liquid characterized by a distribution coefficient in excess of 1.0 for lactic acid and lactic acid salt in said liquid versus water; (f) separating said water-immiscible phase from the mixture formed in step (e); (g) contacting said water-immiscible liquid from step (f) with a material selected from the group consisting of aqueous ammonium hydroxide, solid alkalis, solid alkaline earth compounds, and aqueous non-homogenous suspensions of solid alkalis or solid alkaline earth compounds for a sufficient time and temperature, whereby lactic acid and lactic acid salt are removed from said water-immiscible phase.
Claim 5
Dependent Claim
22 words
A process according to claim 1 or 2 wherein in step (a) said pH is in the range of 2.0 to 5.0.
Claim 6
Dependent Claim
24 words
A process according to claim 1 or 2 wherein in steps (a) and (b) said pH is 4.0 and said temperature is 60° C.
Claim 7
Dependent Claim
25 words
A process according to claim 1 or 2 wherein in step (b) said smaller peptides and amino acids are soluble in 5% aqueous trichloroacetic acid.
Claim 8
Dependent Claim
31 words
A process according to claim 4 wherein said step (a) comprises ultrafiltering whole whey and adding mineral acid to said composition in an amount sufficient to attain said pH of 4.0.
Claim 9
Dependent Claim
21 words
A process according to claim 1 or 2 further comprising adding nutritional supplements to said composition prior to said step (a).
Claim 10
Dependent Claim
20 words
A process according to claim 1 or 2 further comprising heat-sterilizing the composition from step (b) prior to step (c).
Claim 11
Dependent Claim
20 words
A process according to claim 1 or 2 further comprising filter-sterilizing the composition from step (b) priior to step (c).
Claim 12
Dependent Claim
28 words
A process according to claim 1 or 2 further comprising adding acids, bases or neutral salts to the composition from step (b) which increase the ionic strength thereof.
Claim 13
Dependent Claim
44 words
A process according to claim 1 or 2 wherein in step (c) said lactic acid or lactic acid salt-producing microorganism is a microorganism that produces primarily D(-)lactic acid or lactate, L(+)lactic acid or lactate, or a D(-)L(+) racemic mixture of lactic acid or lactate.
Claim 14
Dependent Claim
30 words
A process according to claim 1 or 2 wherein in step (c) said lactic acid or lactic acid salt-producing microorganism is a species selected from the genus Lactobacillus or Streptococcus.
Claim 15
Dependent Claim
25 words
A process according to claim 1 or 2 wherein in step (d) said removal of said cells from said broth is accomplished by cross-flow microfiltration.
Claim 16
Dependent Claim
35 words
A process according to claim 1 or 2 wherein in step (d) said removal of said cells from said broth is accomplished by ultrafiltration with a filter whose molecular weight cutoff is greater than 100,000.
Claim 17
Dependent Claim
24 words
A process according to claim 1 or 2 wherein in step (d) said removal of said cells from said broth is accomplished by centrifugation.
Claim 18
Dependent Claim
44 words
A process according to claim 1 or 2 further comprising the step of increasing the ionic salt concentration of said aqueous solution prior to step (e) by adding a salt selected from the group consisting of ammonium, alkali, alkaline earth chlorides, phosphates, and sulfates.
Claim 19
Dependent Claim
26 words
A process according to claim 1 or 2 wherein in step (e) said product-containing stream is at a pH in the range of 0.5 to 6.0.
Claim 20
Dependent Claim
31 words
A process according to claim 1 or 2 wherein in step (e) said water-immiscible organic solvent is selected from the group consisting of C8 to C14 aliphatic ketones and halogenated hydrocarbons.
Claim 21
Dependent Claim
18 words
A process according to claim 1 or 2 wherein in step (g) said material comprises aqueous ammonium hydroxide.
Claim 22
Dependent Claim
25 words
A process according to claim 1 or 2 wherein said step (g) comprises contacting said water immiscible phase with solid alkali or alkaline earth compound.
Claim 23
Dependent Claim
29 words
A process according to claim 20 wherein said alkali or alkaline earth compound is selected from the group consisting of calcium, magnesium, iron, zinc, aluminum hydroxides, oxides and carbonates.
Claim 24
Dependent Claim
40 words
A process according to claim 1 or 2 further comprising the step of, prior to said step (e), contacting said stream with an ion exchange resin to adjust said stream to a pH in the range of 0.5 to 6.0.
Claim 25
Dependent Claim
25 words
A process according to claim 1 or 2 wherein in step (e) said tertiary amine comprises a trialkyl amine and said solvent comprises isobutyl-heptyl ketone.
Claim 26
Dependent Claim
24 words
A process according to claim 1 or 2 wherein in step (e) said tertiary amine comprises a trialkyl amine and said solvent comprises 2-octanone.
Claim 27
Dependent Claim
19 words
A process according to claim 23 wherein said step (g) comprises contacting said water-immiscible phase with aqueous ammonium hydroxide.
Claim 28
Dependent Claim
26 words
A process according to claim 23 wherein said step (g) comprises contacting said water-immiscible phase with said aqueous suspension of said alkali or alkaline earth compound.
Claim 29
Dependent Claim
32 words
A process according to claim 1 or 2 wherein in step (e) said tertiary amine comprises a trialkyl amine and said solvent comprises a mixture of a ketone and a phosphoryl oxide.
Claim 30
Dependent Claim
35 words
A process according to claim 1 or 2 wherein in said step (g) said contact occurs at the same or at a lower temperature than the temperature at which the extraction step (e) is performed.
Claim 31
Dependent Claim
14 words
A process according to claim 1 or 2 wherein said lactic acid is heat-stable.
References Cited (Backward Citations)
US1540951A
Cited
US1704458A
Cited
US2539472A
Cited
US2710880A
Cited
US2838443A
Cited
US2885436A
Cited
US3036918A
Cited
US3284495A
Cited
US4275234A
Cited
US4001437A
Cited
US4016295A
Cited
US3944606A
Cited
US4036999A
Cited
US4364962A
Cited
US4291007A
Cited
US4427658A
Cited
US4334095A
Cited
US4444881A
Cited
WO1984001104A1
Cited
US4529611A
Cited
US4500549A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-10-05 | 1991-04-06 | 1991-10-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-10-05 | 1995-04-06 | 1995-10-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-10-05 | 1999-04-06 | 1999-10-06 | $7700.00 | Window Closed / Lapsed |