US4169013A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing glucoamylase
Assignee: Genencor International Wisconsin Inc
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Filing: 1976-07-28
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Granted: 1979-09-25
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Expires: 1996-07-28
Abstract
Abstract Glucoamylase is prepared by fermenting a microorganism capable of producing glucoamylase in a nutrient medium containing at least about 16% to about 25% of ground corn which has been liquefied by the action of heat, water and an alpha-amylase enzyme preparation. The alpha-amylase enzyme preparation is preferably derived from a microorganism of Bacillus licheniformis.
Inventors
- 👤 Jay A. Smith
- 👤 Jeffrey R. Frankiewicz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 20:18
CPC Classifications
C; C12; C12N; C12N9/00; C12N9/14; C12N9/24; C12N9/2402; C12N9/2405; C12N9/2408; C12N9/2411; C12N9/2428; Y; Y10; Y10S; Y10S435/00; Y10S435/8215; Y10S435/911; Y10S435/913; Y10S435/917
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
298 words
In a process for the production of glucoamylase comprising, cultivating a culture of a glucoamylase-producing microorganism in a pre-sterilized nutrient medium under aeration in a plurality of development stages and thereafter inoculating, in a final development stage, the last culture development stage (seed stage) of glucoamylase-producing microorganisms in a pre-sterilized fermentation medium comprising a carbon source in the form of carbohydrates and a nitrogen source, wherein the carbon source comprises enzymatically liquified ground corn, and fermenting the innoculated pre-sterilized fermentation medium to thereby obtain the glucoamylase enzyme, the improvement comprising: preparing the sterilized fermentation medium by the steps comprising: (1) forming a fermentation medium by admixing ground corn as a primary carbon source, a primary nitrogen source and water at a temperature ranging from about 20° C. to about 60° C.; (2) heating the medium in step (1) by the action of steam to a temperature in the range from about 55° C. to about 80° C. and at a pH in the range from about 4.5 to about 7.5 in the presence of a bacterial alpha-amylase preparation derived from a Bacillus licheniformis microorganism, said bacterial alpha-amylase enzyme preparation being added to the medium before or during the steam heating of the medium for a time sufficient to substantially liquify all the ground corn (3) further heating the medium by the action of steam at a temperature of at least 100° C. and holding the medium at this temperature to sterilize the medium; and (4) cooling the medium to thereby obtain a sterilized fermentation medium containing enzymatically liquified ground corn having a solids content greater than about 16% and up to about 25% by weight dry substance basis which is inoculated with the development stage (seed stage) of glucoamylase-producing microorganism to produce glucoamylase by fermentation in said medium.
Claim 2
Dependent Claim
298 words
In a process for the production of glucoamylase comprising, cultivating a culture of a glucoamylase-producing microorganism in a pre-sterilized nutrient medium under aeration in a plurality of development stages and thereafter inoculating, in a final development stage, the last culture development stage (seed stage) of glucoamylase-producing microorganisms in a pre-sterilized fermentation medium comprising a carbon source in the form of carbohydrates and a nitrogen source, wherein the carbon source comprises enzymatically liquified ground corn, and fermenting the innoculated pre-sterilized fermentation medium to thereby obtain the glucoamylase enzyme, the improvement comprising: preparing the sterilized fermentation medium by the steps comprising: (1) forming a fermentation medium by admixing ground corn as a primary carbon source, a primary nitrogen source and water at a temperature ranging from about 20° C. to about 60° C.; (2) heating the medium in step (1) by the action of steam to a temperature in the range from about 55° C. to about 80° C. and at a pH in the range from about 4.5 to about 7.5 in the presence of a bacterial alpha-amylase preparation derived from a Bacillus licheniformis microorganism, said bacterial alpha-amylase enzyme preparation being added to the medium before or during the steam heating of the medium for a time sufficient to substantially liquify all the ground corn (3) further heating the medium by the action of steam at a temperature of at least 100° C. and holding the medium at this temperature to sterilize the medium; and (4) cooling the medium to thereby obtain a sterilized fermentation medium containing enzymatically liquified ground corn having a solids content greater than about 16% and up to about 25% by weight dry substance basis which is inoculated with the development stage (seed stage) of glucoamylase-producing microorganism to produce glucoamylase by fermentation in said medium.
Claim 3
Dependent Claim
28 words
The process in accordance with claim 1, wherein enzymatically liquefied ground corn has a solids content in the range from about 18% to about 22%, dry substance basis.
Claim 4
Dependent Claim
23 words
The process in accordance with claim 1, wherein the enzymatically liquefied ground corn has a solids content of about 20%, dry substance basis.
Claim 5
Dependent Claim
46 words
The process in accordance with claim 1, wherein said bacterial alpha-amylase enzyme preparation is derived from a microorganism selected from the group consisting of Bacillus licheniformis NCIB 8061, NCIB 8059, ATCC No. 6598, ATCC No. 6634, ATCC No. 8480, ATCC No. 9945a and ATCC No. 11945.
Claim 6
Dependent Claim
16 words
The process in accordance with claim 1, wherein said glucoamylase-producing microorganism is derived from Aspergillus niger.
Claim 7
Dependent Claim
14 words
The process in accordance with claim 5, wherein said microorganism is a mutant strain.
Claim 8
Dependent Claim
24 words
The process in accordance with claim 1, wherein the fermentation is conducted at a pH in the range from about 3.5 to about 6.0.
Claim 9
Dependent Claim
15 words
The process of claim 1, wherein the primary nitrogen source comprises corn steep liquor solids.
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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) | 1982-09-24 | 1983-03-26 | 1983-09-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-09-24 | 1987-03-26 | 1987-09-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-09-24 | 1991-03-26 | 1991-09-25 | $7700.00 | Window Closed / Lapsed |