US2006252137A1PendingUtilityA1
Ethanol fermentation using oxidation reduction potential
Individually held — no corporate assignee on recordPriority: Dec 1, 2004Filed: Jul 13, 2006Published: Nov 9, 2006
Est. expiryDec 1, 2024(expired)· nominal 20-yr term from priority
Inventors:Brian Burmaster
Y02E50/10C12P 7/06
49
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Claims
Abstract
A process to improve ethanol yield, decrease fermentation time and reduce byproduct formation by monitoring and controlling oxidation reduction potential (redox) of the fermentor is disclosed.
Claims
exact text as granted — not AI-modified1 . An anaerobic fermentation system to produce ethanol, which monitors controls or adjusts the oxidation reduction potential in order to attain maximum ethanol yields and/or productivity.
2 . The process as defined in claim 1 wherein the ethanol producing oxidation reduction potential is controlled within the limits of −250 millivolts to +50 millivolts.
3 . The process according to claim 1 , wherein either anhydrous ammonia or aqueous ammonia is substituted for sodium hydroxide, in the form of soda ash or caustic solution.
4 . The process according to claim 2 , wherein either anhydrous ammonia or aqueous ammonia is substituted for sodium hydroxide, in the form of soda ash or caustic solution.
5 . The process according to claim 1 , wherein sulfite, bi-sulfite or sulfur dioxide is oxidized or removed to elevate oxidation reduction potential.
6 . The process according to claim 2 , wherein sulfite, bi-sulfite or sulfur dioxide is oxidized or removed to elevate oxidation reduction potential.
7 . The process according to claim 1 , wherein air or oxygen is sparged in the feed to the fermentation liquid prior to raise the oxidation reduction potential.
8 . The process according to claim 2 , wherein air or oxygen is sparged in the feed to the fermentation liquid prior to raise the oxidation reduction potential.
9 . The process according to claim 1 , wherein air or oxygen is sparged directly into the fermentor.
10 . The process according to claim 2 , wherein air or oxygen is sparged directly into the fermentor.
11 . The process according with claim 1 wherein an oxidant, such as hydrogen peroxide, is added to the fermentation liquid in order to raise the oxidation reduction potential.
12 . The process according with claim 2 wherein an oxidant, such as hydrogen peroxide, is added to the fermentation liquid in order to raise the oxidation reduction potential.
13 . The process according to claim 1 wherein the yeast used for ethanol fermentation is Saccharomyces Cerevisiae.
14 . The process according to claim 2 wherein the yeast used for ethanol fermentation is Saccharomyces Cerevisiae.
15 . The process according to claim 1 wherein the fermentor is in the continuous or batch mode.
16 . The process according to claim 2 wherein the fermentor is in the continuous or batch mode.
17 . A process according to claim 1 wherein the yeast viability count is maintained within certain limits by adjusting the oxidation reduction potential.
18 . A process according to claim 2 wherein the yeast viability count is maintained within certain limits by adjusting the oxidation reduction potential.
19 . A process according to claim 1 wherein the residual starch content of the mash is reduced by optimizing the oxidation reduction potential.
20 . A process according to claim 2 wherein the residual starch content of the mash is reduced by optimizing the oxidation reduction potential.
21 . A process for efficiently producing ethanol through application of anaerobic fermentation comprising:
a. providing a closed vessel having both an inlet and outlet, and at least one feed inlet for introducing of fermentable mash into the vessel; b. said fermentable mash having a percentage of ingredients selected from the group including at least one of corn, milo, barley, wheat, oats, sugar cane, and molasses; c. said fermentable mash including water in an amount between about 55% to 90% by weight; d. adding an enzyme into the mash-water mixture to initiate the enzymatic breakdown of the starch content of the mash; e. adding a yeast into the mixture to further initiate the fermentation process; f. aerating the fermenting mash in the vessel through the addition of pressurized air or oxygen into the contained mash; g. continuing the aeration of the aqueous mash solution in the closed vessel and determining the oxidation-reduction potential of the fermenting mash and maintaining a voltage potential between about −250 millivolts to +50 millivolts to attain the most efficient fermentation of the mash to achieve the maximum ethanol yield.
22 . The process of claim 21 wherein the oxidation-reduction potential of the fermentable mash is elevated in ph through reductant substitution by decreasing of ammonia through the addition of a caustic solution.
23 . The process of claim 21 wherein the sulfite, bi-sulfite or sulfur dioxide in the mash are oxidized through said addition of air or oxygen to elevate the oxidation-reduction potential of the fermentable mash.
24 . The process of claim 21 wherein an oxidant, such as hydrogen peroxide, is added to the fermentable mash in order to raise the oxidation-reduction potential of the fermentable mash.Join the waitlist — get patent alerts
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