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Methods for fermenting carbohydrate-rich crops

a technology of carbohydrate-rich crops and methods, applied in the direction of fermentation, biofuels, etc., can solve the problems of 34° c temperature rise, high capital investment, and inability to cool the fermentation medium,

Inactive Publication Date: 2016-03-10
HAMRICK EDWARD BRIAN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent text describes the results of fermenting sugar beet using different methods. The researchers found that the amount of gas produced and the sample size had a significant impact on the overall sugar conversion yield. Slow infusion was found to be slightly detrimental, while adding pectinase enzyme improved the fermentation. This patent also shows that the vacuum infusion method can deliver in situ enzymatic and microbiological activity without mechanical mixing and minimum preprocessing of the biomass.

Problems solved by technology

This means that fermenting an 18% sugar solution will result in a temperature rise of 34° C., which means that cooling of the fermentation medium is required.
All of these techniques are quite capital-intensive.
The parenchyma cells are packed tightly together, but there are small gaps between them because the packing is imperfect.
This causes the contents of the vacuoles to leak out of the parenchyma cells and causes enzymes to more easily diffuse into the vacuoles.
Pectate lyase and polygalacturanase, when they degrade pectin, also produce methanol which is often an undesirable product when producing ethanol.
One significant problem with current techniques for fermenting sugars to ethanol is bacterial contamination, in particular contamination by Lactobacillus.
Without wishing to be bound by any particular theory, it is believed that turbulent mixing propagates bacteria throughout the fermentation medium, and since the contaminating bacteria can out-compete yeast, there is significant contamination.
Because the parenchyma cells are so small, it takes a lot of energy to crush them or to extract the sugar from them with hot water.
Almost 35% of the capital and operating costs of producing sugar from stalks is due to the cost of crushing.
Similarly, much of the cost of producing sugar from sugar beets is due to the cost of hot water extraction.
Since transportation costs are primarily a function of volume (and not weight), and since crops are often harvested significant distances from where they're processed, it is quite expensive to transport sugars at such low densities since only 5% to 10% of the volume of a truck is taken up by sugar.
Since the outer layer of the sugar beets are often abraded and damaged by harvesting, microorganisms can more easily penetrate the outer layers of the sugar beet, leading to sugar losses due to fermentation to lactic acid and acetic acid.
Similarly, sugar cane, sweet sorghum and tropical maize hybrid are more susceptible to microorganisms penetrating the pith because the cane has been cut open into billets during harvesting.
Much of the capital cost and operating cost of producing ethanol from carbohydrate-rich crops is the cost of heating the feedstock.
Another significant capital cost and operating cost of producing ethanol from carbohydrate-rich crops is the cost of cooling the fermentation reactor.

Method used

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  • Methods for fermenting carbohydrate-rich crops

Examples

Experimental program
Comparison scheme
Effect test

example 1

Infusion of Water into Sugar Beet Parenchyma Tissue

[0116]Slices of sugar beet were cut radially to three different thicknesses, 6 mm, 12 min and 18 mm. These slices were then cut into 25 mm square slices and all of the 25 mm square slices for each of the three thicknesses were weighed and put into three of the apparatus described above (FIG. 1). The gas cap was air for this example.

[0117]In Phase 1, a vacuum of 13 kPa was applied for 30 minutes, free water was removed, pressure was restored to 100 kPa and each cube was weighed.

[0118]In Phase 2, a vacuum of 13 kPa was applied for 30 minutes, water was infused under vacuum until the cube was covered, pressure was restored to 100 kPa, water infused into the parenchyma tissue for 30 minutes, free water was removed and then each cube was weighed.

[0119]In Phase 3, a vacuum of 13 kPa was applied for 30 minutes, free water was removed, pressure was restored to 100 kPa and each cube was weighed.

[0120]The result of this test are shown in Tabl...

example 2

Fermentation of Sugar Cane

[0121]Chopped sugar cane was infused with a slightly acidic yeast solution enriched with nitrogen-rich nutrients (Fermax from the BSG Corporation). Two different solutions were tested in duplicate, one using Thermosacc yeast and one using Distillamax yeast. Both yeasts are commercially available from Lallemand Biofuels & Distilled Spirits and differ in the average size of the cell bodies. The Thermosacc yeast has an average cell diameter of 5 microns and the Distillamax has an average cell diameter of 10 microns. After infusion was completed the carbon dioxide production was monitored through gas counters to estimate the fermentation progress. The following procedure was used:

[0122]1. Start heating thermostatic bath to 38° C.

[0123]2. Weigh approximately 50 g of sugar cane, then chop up into approximately one inch pieces, weighing the total amount of cane again after chopping.

[0124]3. Prepare two yeast solutions, one with 5 g / L Distillamax yeast, 1 g / L Ferma...

example 3

Fermentation of Sugar Beet

[0132]Coarsely chopped sugar beet pieces were infused with a slightly acidic yeast solution made Distillamax yeast by Lallemand Biofuels & Distilled Spirits. Different infusion times were used for each sample. After infusion was completed, the carbon dioxide production was monitored by the gas counters to estimate the fermentation progress. The following procedure was used:

[0133]1. Ensure that the thermostatic bath is at 38° C.

[0134]2. Weigh approximately 100 g of sugar beets, then chop up into pieces of approximately one-inch cubes, weighing the total beet again after chopping.

[0135]3. Prepare yeast solution with 5 g / L Distillamax yeast, buffering to a pH of 3.5 with phosphoric acid.

[0136]4. In the solution for samples 2 and 4 add an enzyme with pectinase activity at a loading of about 5 g per kg of dry biomass.

[0137]5. Place sugar beet sample in sealed beakers in the thermostatic bath, and apply vacuum for 30 min.

[0138]6. Infuse enough solution to submerg...

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Abstract

A method for fermenting carbohydrate-rich crops is provided. Sugar beet, sugar cane, sweet sorghum, tropical maize hybrids and fruits are rich in simple sugars; potato, sweet potato, cassava and yam are rich in starch; and Jerusalem artichoke is rich in inulin. This method uses vacuum infusion to infuse yeast into the intercellular space (apoplast) of the parenchyma tissue. The simple sugars diffuse into the apoplast, come into contact with the yeast and produce ethanol. Ethanol can be extracted from the crop by vacuum stripping or crushing or can be left inside the starchy crop to preserve it. In some variants, pectinase enzymes degrade the parenchyma cell walls to speed up diffusion of simple sugars to the yeast, speed up diffusion of amylase to starch granules or speed up diffusion of inulinase to insoluble inulin.

Description

PRIORITY DATA[0001]This patent application is a non-provisional application with priority to U.S. Provisional Patent App. No. 62 / 127,637, filed Mar. 3, 2015, and to U.S. Provisional Patent App. No. 62 / 139,881, filed Mar. 30, 2015, each of which is hereby incorporated by reference herein.FIELD OF THE INVENTION[0002]The present invention generally relates to methods for fermenting carbohydrate-rich crops.BACKGROUND OF THE INVENTION[0003]Many fermentation organisms convert carbohydrates to ethanol. The most widely used fermentation organisms, brewer's yeast and baker's yeast, are strains of Saccharomyces cerevisiae. Ethanol has significant economic value as beverages, transportation fuels and precursors for other organic compounds.[0004]Fermentation organisms can directly convert glucose, fructose, maltose (glucose dimer) and sucrose (glucose-fructose dimer) to ethanol. Herein, monomers and dimers of glucose and fructose will be referred to as simple sugars and fermentation organisms t...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C12P7/14
CPCC12P7/14C12P7/06C08B37/0003C08B30/04C08B37/0054Y02E50/10
Inventor HAMRICK, EDWARD, BRIAN
Owner HAMRICK EDWARD BRIAN
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